JPH04325692A - Method for recovering metal by electrolysis - Google Patents
Method for recovering metal by electrolysisInfo
- Publication number
- JPH04325692A JPH04325692A JP12490691A JP12490691A JPH04325692A JP H04325692 A JPH04325692 A JP H04325692A JP 12490691 A JP12490691 A JP 12490691A JP 12490691 A JP12490691 A JP 12490691A JP H04325692 A JPH04325692 A JP H04325692A
- Authority
- JP
- Japan
- Prior art keywords
- cathode
- metal
- electrolysis
- bag
- electrolyte
- 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
Links
- 239000002184 metal Substances 0.000 title claims abstract description 31
- 229910052751 metal Inorganic materials 0.000 title claims abstract description 31
- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 22
- 238000000034 method Methods 0.000 title claims description 11
- 150000002739 metals Chemical class 0.000 claims abstract description 9
- 239000003014 ion exchange membrane Substances 0.000 claims abstract description 7
- 239000008151 electrolyte solution Substances 0.000 claims description 15
- 238000011084 recovery Methods 0.000 claims description 2
- 239000007788 liquid Substances 0.000 abstract description 6
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 abstract description 2
- 239000003456 ion exchange resin Substances 0.000 abstract description 2
- 229920003303 ion-exchange polymer Polymers 0.000 abstract description 2
- 150000002500 ions Chemical class 0.000 abstract description 2
- 239000003792 electrolyte Substances 0.000 abstract 4
- 150000001455 metallic ions Chemical class 0.000 abstract 2
- 230000008021 deposition Effects 0.000 abstract 1
- 239000000725 suspension Substances 0.000 abstract 1
- 238000005406 washing Methods 0.000 abstract 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 4
- 229910021645 metal ion Inorganic materials 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- TXUICONDJPYNPY-UHFFFAOYSA-N (1,10,13-trimethyl-3-oxo-4,5,6,7,8,9,11,12,14,15,16,17-dodecahydrocyclopenta[a]phenanthren-17-yl) heptanoate Chemical compound C1CC2CC(=O)C=C(C)C2(C)C2C1C1CCC(OC(=O)CCCCCC)C1(C)CC2 TXUICONDJPYNPY-UHFFFAOYSA-N 0.000 description 1
- IDCBOTIENDVCBQ-UHFFFAOYSA-N TEPP Chemical compound CCOP(=O)(OCC)OP(=O)(OCC)OCC IDCBOTIENDVCBQ-UHFFFAOYSA-N 0.000 description 1
- 229910021626 Tin(II) chloride Inorganic materials 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 238000005341 cation exchange Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000002923 metal particle Substances 0.000 description 1
- 239000002952 polymeric resin Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 235000011150 stannous chloride Nutrition 0.000 description 1
- 239000001119 stannous chloride Substances 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Electrolytic Production Of Metals (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は、イオン交換樹脂を隔膜
として電解法で電解する液中のイオン化している金属を
回収する方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for recovering ionized metals from an electrolytic solution using an ion exchange resin as a diaphragm.
【0002】0002
【従来の技術とその問題点】従来、イオン交換膜を隔膜
として用い、陰極側にイオン化している金属を含有する
電解する液を供給して電解し、陰極に析出した金属を取
り出すという方法が行われていた。しかし、陰極に析出
する金属が多くなると陰極に析出した金属が脱落して、
陰極槽内の底部に堆積するため析出した金属を取り出し
するのに手間がかかることや、又は脱落した金属が微粒
子となり浮遊してイオン交換膜に付着したりして電解操
作が継続できなくなる等の問題が生じている。さらに、
電解する液が多い場合に小さな電解槽で電解を行うには
、電解槽の近くに電解するための液を貯留する槽を設置
し、該貯留槽と電解槽の陰極槽を導管でつなぎ、ポンプ
で陰極槽から排出した液量分を貯留槽から供給するとい
う循環型の電解を行う際には、電解により陰極に析出し
た金属が脱落し浮遊すると、ポンプの詰まりの原因とな
る他に導管に堆積して循環できなくなるという問題もあ
る。[Prior art and its problems] Conventionally, there has been a method in which an ion exchange membrane is used as a diaphragm, an electrolytic solution containing ionized metal is supplied to the cathode side, electrolysis is carried out, and the metal deposited on the cathode is taken out. It was done. However, when the amount of metal deposited on the cathode increases, the metal deposited on the cathode falls off.
The metal deposited at the bottom of the cathode chamber may take time to remove, or the fallen metal may become fine particles that become suspended and adhere to the ion exchange membrane, making it impossible to continue the electrolytic operation. A problem has arisen. moreover,
To perform electrolysis in a small electrolytic tank when there is a large amount of liquid to be electrolyzed, install a tank near the electrolytic tank to store the liquid to be electrolyzed, connect the storage tank to the cathode cell of the electrolytic tank with a conduit, and use a pump. When carrying out circulation type electrolysis in which the amount of liquid discharged from the cathode bath is supplied from the storage tank, if the metal deposited on the cathode falls off and floats, it may clog the pump and cause damage to the conduit. There is also the problem that it accumulates and cannot be circulated.
【0003】0003
【発明の目的】本発明は、上記従来法の欠点を解決する
ために成されたもので、陰極に析出し脱落した金属を取
り出す操作を簡便にすることと、浮遊させることを解消
し、循環型の電解を長時間行なえるようにする電解によ
る金属回収方法を提供することを目的とする。OBJECTS OF THE INVENTION The present invention has been made to solve the above-mentioned drawbacks of the conventional method. The object of the present invention is to provide a method for recovering metals by electrolysis, which allows mold electrolysis to be carried out for a long time.
【0004】0004
【課題を解決するための手段】本発明は、電解する液中
にイオン化している金属をイオン交換膜で陽極と陰極を
隔てた電解法で金属回収する際に、該電解する液の通過
が自由に行われる程度の目または孔のある袋の中に陰極
を入れて電解し、電解中に陰極を入れた袋の外側の電解
する液を対流または移動させながら行うことを特徴とす
る電解による金属回収方法である。[Means for Solving the Problems] The present invention provides a method for recovering metals ionized in an electrolytic solution using an electrolytic method in which an anode and a cathode are separated by an ion exchange membrane. Electrolysis is carried out by placing a cathode in a bag with holes or holes that allow the electrolysis to occur freely, and during electrolysis, the electrolytic solution outside the bag containing the cathode is carried out by convection or movement. This is a metal recovery method.
【0005】前記電解する液の通過が自由に行われる程
度の目または孔のある袋として、その材質は電解する液
に腐食されないものを用いる必要があり、各種の高分子
樹脂製のものが適用される。また、電解する液が自由に
通過する程度としては、市販されている合成繊維製の濾
布が入手も容易であり使用しやすく、使用に際して二重
に重ねて使用することもできる。他に、電解する液の質
と析出し、脱落する金属の粒子の状態にもよるが、おお
むね0.3〜0.5ミクロン程度の孔のある樹脂シート
を用いることもできる。なお、該袋の中に陰極を入れて
電解するが、袋と陰極とは接触しない状態で保持するよ
うにした方がより好ましいものである。[0005] As for the bag having holes or holes large enough to allow the electrolytic solution to freely pass through, it is necessary to use a material that will not be corroded by the electrolytic solution, and materials made of various polymer resins can be used. be done. In addition, commercially available synthetic fiber filter cloths are easily available and easy to use, and can be used in a double layered manner to allow the electrolytic solution to freely pass through. Alternatively, a resin sheet with pores of approximately 0.3 to 0.5 microns may also be used, depending on the quality of the electrolytic solution and the state of the metal particles that precipitate and fall off. Although the cathode is placed in the bag for electrolysis, it is more preferable to hold the bag and the cathode in a state where they do not come into contact with each other.
【0006】電解中に陰極を入れた袋の外側の電解する
液を対流または移動させながら行うのは、電解条件を安
定して行うためで、電解する液中の金属イオン濃度が低
くなる陰極付近への金属イオンの供給と袋の目や孔の詰
まりを防ぐこと、さらに金属以外のイオンを速やかにイ
オン交換膜付近に到達させる効果があるからである。[0006] During electrolysis, the electrolytic solution outside the bag containing the cathode is moved by convection to maintain stable electrolytic conditions, and the concentration of metal ions in the electrolytic solution is low near the cathode. This is because it has the effect of supplying metal ions to the membrane and preventing clogging of the openings and pores of the bag, as well as allowing ions other than metal to quickly reach the vicinity of the ion exchange membrane.
【0007】以下、本発明に係わる実施例を記載するが
、該実施例は本発明を限定するものではない。[0007] Examples related to the present invention will be described below, but the examples are not intended to limit the present invention.
【0008】[0008]
【実施例】陽イオン交換膜(旭硝子製:CMV型式)を
用い陰極槽と陽極槽に隔てた電解槽の陰極槽に電解する
液を供給するポンプと導管と陰極槽から電解したのちの
液を排出する導管が接続去れた貯留槽から成る装置を用
い、電解する液として塩化第一スズ溶液(Snとして1
4g/l含有)を循環するようにし、陽極槽には2.5
mol希硫酸を満たし、陽極はDSE(不溶性金属電極
)を用い、陰極はチタン製の板とし、その陰極は市販の
濾布(テトロン)を袋に加工した中に入れ、電解条件は
3V、60Aで電解した。電解時間18時間後に陰極を
入れた袋を取り出し、そのまま水洗して金属スズを回収
した。なお、電解した液中のスズ濃度は1g/lとなり
、液中に金属スズが浮遊したり、陰極槽内に堆積するこ
とはなかった。[Example] Using a cation exchange membrane (manufactured by Asahi Glass: CMV model), the electrolytic tank is separated into a cathode tank and an anode tank. Using a device consisting of a storage tank to which a discharge conduit is connected, a stannous chloride solution (Sn: 1
(containing 4 g/l), and 2.5 g/l in the anode tank.
mol dilute sulfuric acid, a DSE (insoluble metal electrode) was used as the anode, a titanium plate was used as the cathode, and the cathode was placed in a bag made of commercially available filter cloth (Tetron).The electrolytic conditions were 3V and 60A. I electrolyzed it. After 18 hours of electrolysis, the bag containing the cathode was taken out and washed with water to recover the metal tin. The tin concentration in the electrolyzed solution was 1 g/l, and no metal tin was floating in the solution or deposited in the cathode bath.
【0009】[0009]
【従来例】陰極を袋に入れずに実施例と同様に電解した
ところ、電解時間20時間後に排出用導管が詰まり電解
槽から電解液が流出してしまった。また、陰極槽の底に
金属スズが堆積していた。[Conventional example] When electrolysis was carried out in the same manner as in the example without placing the cathode in a bag, the discharge conduit was clogged after 20 hours of electrolysis time, and the electrolytic solution flowed out from the electrolytic cell. Metallic tin was also deposited on the bottom of the cathode tank.
【0010】0010
【発明の効果】以上の説明で明らかのように、本発明の
方法によれば、従来法では特に循環しながら電解する液
中の金属イオンを陰極に析出させる場合に、陰極に析出
した金属が脱落して陰極槽内に堆積することや浮遊して
、貯留槽等と接続している導管の詰まりやポンプの詰ま
り等の影響を与える他に堆積した金属を取り出しするに
手間がかかることがあったことを、すべて解決すること
ができると共に、電解して回収した金属をそのまま洗浄
できるという効果もあり、極めて工業的に有用なものと
いえる。Effects of the Invention As is clear from the above explanation, according to the method of the present invention, metals deposited on the cathode can be deposited on the cathode, especially when the metal ions in the circulating electrolytic solution are deposited on the cathode in the conventional method. Metals may fall off and accumulate in the cathode tank, or they may float and cause clogging of conduits connected to storage tanks, clogging of pumps, etc., and it may take time and effort to remove the deposited metals. In addition to being able to solve all of these problems, this method also has the effect of allowing metals recovered by electrolysis to be cleaned as they are, making it extremely useful industrially.
Claims (1)
をイオン交換膜で陽極と陰極を隔てた電解法で金属回収
する際に、該電解する液の通過が自由に行われる程度の
目または孔のある袋の中に陰極を入れて電解し、電解中
に陰極を入れた袋の外側の電解する液を対流または移動
させながら行うことを特徴とする電解による金属回収方
法。Claim 1: When recovering metals ionized in the electrolytic solution using an electrolytic method in which an anode and a cathode are separated by an ion exchange membrane, the electrolytic solution can freely pass through the metal or the metal. A metal recovery method by electrolysis, characterized in that electrolysis is carried out by placing a cathode in a bag with holes, and during electrolysis, the electrolytic solution outside the bag in which the cathode is placed is caused to flow or move.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12490691A JPH04325692A (en) | 1991-04-26 | 1991-04-26 | Method for recovering metal by electrolysis |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12490691A JPH04325692A (en) | 1991-04-26 | 1991-04-26 | Method for recovering metal by electrolysis |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04325692A true JPH04325692A (en) | 1992-11-16 |
Family
ID=14897042
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12490691A Pending JPH04325692A (en) | 1991-04-26 | 1991-04-26 | Method for recovering metal by electrolysis |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04325692A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009074131A (en) * | 2007-09-20 | 2009-04-09 | Dowa Metals & Mining Co Ltd | Electrowinning method for tin |
-
1991
- 1991-04-26 JP JP12490691A patent/JPH04325692A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009074131A (en) * | 2007-09-20 | 2009-04-09 | Dowa Metals & Mining Co Ltd | Electrowinning method for tin |
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