JP3144906B2 - Method for removing fluorine ions from zinc electrolyte - Google Patents

Method for removing fluorine ions from zinc electrolyte

Info

Publication number
JP3144906B2
JP3144906B2 JP23898692A JP23898692A JP3144906B2 JP 3144906 B2 JP3144906 B2 JP 3144906B2 JP 23898692 A JP23898692 A JP 23898692A JP 23898692 A JP23898692 A JP 23898692A JP 3144906 B2 JP3144906 B2 JP 3144906B2
Authority
JP
Japan
Prior art keywords
zinc
fluorine ions
electrolyte
zinc electrolyte
fluorine
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.)
Expired - Fee Related
Application number
JP23898692A
Other languages
Japanese (ja)
Other versions
JPH0657476A (en
Inventor
宗治 大原
俊子 横田
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.)
Mitsui Mining and Smelting Co Ltd
Original Assignee
Mitsui Mining and Smelting Co Ltd
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 Mitsui Mining and Smelting Co Ltd filed Critical Mitsui Mining and Smelting Co Ltd
Priority to JP23898692A priority Critical patent/JP3144906B2/en
Publication of JPH0657476A publication Critical patent/JPH0657476A/en
Application granted granted Critical
Publication of JP3144906B2 publication Critical patent/JP3144906B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Removal Of Specific Substances (AREA)
  • Electrolytic Production Of Metals (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は亜鉛電解液中のフッ素イ
オンを硫酸チタニル・2水塩の加水分解生成物を用いて
吸着除去する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for adsorbing and removing fluorine ions in a zinc electrolyte using a hydrolysis product of titanyl sulfate dihydrate.

【0002】[0002]

【従来の技術およびその問題点】一般に、亜鉛精錬で
は、硫化亜鉛精鉱等をばい焼した亜鉛焼鉱を溶解槽、シ
ックナ、清浄槽等での処理を経た上で、電解槽中で陰極
板上に亜鉛を析出させ、剥ぎ取った後、溶解し、鋳造等
の処理が施される。
2. Description of the Related Art Generally, in zinc refining, zinc ore obtained by roasting zinc sulfide concentrate or the like is treated in a melting tank, thickener, cleaning tank, or the like, and then treated in a cathode plate in an electrolytic cell. After zinc is deposited on the top and stripped off, it is melted and subjected to a process such as casting.

【0003】この亜鉛精錬における電解槽内での処理工
程を継続していくと亜鉛電解液中にフッ素イオンが次第
に蓄積され、フッ素イオン濃度が高まってくる。このフ
ッ素イオンの影響により、カソード側のアルミニウム電
極の表面が腐食され、極端な場合には穴が明いてしま
い、電析した亜鉛が電極から剥離出来なくなり、電極を
廃棄しなければならなかった。そのため、亜鉛電解液中
のフッ素イオン濃度を一定に保つためのフッ素イオン除
去方法が必要になる。
As the processing step in the electrolytic cell in the zinc refining is continued, fluorine ions are gradually accumulated in the zinc electrolyte, and the fluorine ion concentration increases. Under the influence of the fluorine ions, the surface of the cathode-side aluminum electrode was corroded. In an extreme case, a hole was formed, and the deposited zinc could not be separated from the electrode, and the electrode had to be discarded. Therefore, a fluorine ion removing method for maintaining a constant fluorine ion concentration in the zinc electrolyte is required.

【0004】従来、亜鉛電解液中のフッ素イオン濃度が
高くなった場合には、亜鉛電解液の一部を抜き出し、新
規に亜鉛電解液を補充して希釈することによりフッ素イ
オン濃度を定常に保っていた。あるいは、原鉱石中のフ
ッ素イオン濃度を下げるように原料配合して電解液中の
フッ素イオン濃度の低下を待っていた。
Conventionally, when the concentration of fluorine ions in a zinc electrolyte becomes high, a part of the zinc electrolyte is extracted, and a new zinc electrolyte is replenished and diluted to maintain a constant fluorine ion concentration. I was Alternatively, raw materials are blended so as to lower the concentration of fluorine ions in the raw ore, and the reduction of the concentration of fluorine ions in the electrolyte has been awaited.

【0005】しかしながら、亜鉛電解液を廃棄するの
は、亜鉛を損失することであり、コストがかかること、
また廃水処理に負担がかかること等の問題点を有し、さ
らに、原料からフッ素イオン濃度を減らす場合にはフッ
素イオン濃度が低下するまでに時間がかかり、カソード
電極がフッ素により腐食され、亜鉛が電極から剥離し難
くなり、そのためカソード電極からの剥離に多くの人手
を要する問題点が在る。
However, discarding the zinc electrolyte is a loss of zinc, which is costly.
In addition, there is a problem that a burden is imposed on wastewater treatment.In addition, when reducing the fluorine ion concentration from the raw material, it takes time until the fluorine ion concentration decreases, the cathode electrode is corroded by fluorine, and zinc is reduced. There is a problem that peeling off from the electrode becomes difficult, so that much labor is required for peeling off from the cathode electrode.

【0007】本発明は、亜鉛電解液を廃棄することな
く、亜鉛電解液中のフッ素イオンを効率良く除去し得る
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 method capable of efficiently removing fluorine ions in a zinc electrolyte without discarding the zinc electrolyte.

【0006】[0006]

【問題点を解決するための手段】本発明の方法は、亜鉛
電解液中に硫酸チタニル・2水塩を添加し、アルカリp
H調整剤を加えて、好ましくはpHを2.1〜4.2の
範囲に調整して加水分解生成物を生成させ、電解液中の
フッ素イオンを吸着除去させるものであり、これにより
前記問題点を解決したものである。
According to the method of the present invention, titanyl sulfate dihydrate is added to a zinc electrolytic solution, and alkali p is added.
An H adjuster is added to adjust the pH to preferably in the range of 2.1 to 4.2 to generate a hydrolysis product and to adsorb and remove fluorine ions in the electrolytic solution. It is a solution to the point.

【0008】このように本発明は、亜鉛電解液中に硫酸
チタニル・2水塩を添加した後、アルカリpH調整剤に
よりpH調整して得られる加水分解生成物がフッ素イオ
ンを吸着することの知見に基づいて完成したものであ
る。
As described above, the present invention is based on the finding that the hydrolysis product obtained by adding titanyl sulfate dihydrate to a zinc electrolyte and then adjusting the pH with an alkaline pH adjuster adsorbs fluorine ions. It was completed based on

【0009】本発明において、アルカリpH調整剤とし
て、全てのアルカリ性溶液が使用できるが、亜鉛電解液
の汚染を防ぐために、酸化亜鉛水溶液を用いることが好
ましい。そして、これらアルカリpH調整剤により、好
ましくはpHを2.1〜4.2の範囲に調整する。pH
が2.1未満では加水分解生成物が生じず、またpHが
4.2を越えると沈殿物の形態が異なりフッ素イオンが
吸着されない。この発明では、混合時の反応温度は常温
でも良く、また加温してもよい。20〜60℃の加温は
加水分解反応を早める上で好ましい。
In the present invention, any alkaline solution can be used as the alkaline pH adjuster, but it is preferable to use an aqueous zinc oxide solution in order to prevent contamination of the zinc electrolyte. Then, the pH is preferably adjusted to a range of 2.1 to 4.2 with these alkaline pH adjusters. pH
If the pH is less than 2.1, no hydrolysis product is produced, and if the pH exceeds 4.2, the form of the precipitate is different and fluorine ions are not adsorbed. In the present invention, the reaction temperature during mixing may be room temperature or may be heated. Heating at 20 to 60 ° C. is preferable for accelerating the hydrolysis reaction.

【0010】硫酸チタニル・2水塩の添加量は亜鉛電解
液中の亜鉛濃度により、適宜決定され、またその添加に
よるTiは加水分解生成物として回収されるので、電解
液中には残存しない。
The amount of titanyl sulfate dihydrate added is appropriately determined according to the zinc concentration in the zinc electrolyte, and Ti due to the addition is recovered as a hydrolysis product and does not remain in the electrolyte.

【0010】フッ素イオンが吸着された加水分解生成物
は、その後凝集剤を用いて沈殿を凝集させ、濾別するこ
とによりフッ素イオンが電解液中から分離除去される。
以下に、実施例を説明する。
[0010] The hydrolyzate to which the fluorine ions are adsorbed is then coagulated in a precipitate using a coagulant and filtered to separate the fluorine ions from the electrolytic solution.
Hereinafter, examples will be described.

【0011】[0011]

【実施例】亜鉛電解液(亜鉛濃度160g/l)500
mlに、硫酸チタニル・2水塩(5g/l)を添加し、
溶解した。次いで、酸化亜鉛水溶液を加え、その量を変
えることによりpH値を変え、加水分解生成物を生成さ
せた。65℃にて1時間撹拌した後、凝集剤を添加し、
放置後、加水分解生成物を濾過した。その結果を表1に
示す。
EXAMPLES Zinc electrolyte (zinc concentration 160 g / l) 500
ml of titanyl sulfate dihydrate (5 g / l),
Dissolved. Then, an aqueous zinc oxide solution was added, and the pH value was changed by changing the amount thereof, thereby producing a hydrolysis product. After stirring at 65 ° C. for 1 hour, a flocculant was added,
After standing, the hydrolysis product was filtered. Table 1 shows the results.

【0011】 [0011]

【0012】[0012]

【発明の効果】以上のような本発明によれば、フッ素イ
オン濃度が高くなった亜鉛電解液中に硫酸チタニル・2
水塩を添加することによりフッ素イオンをその加水分解
生成物に吸着除去させることが出来るため、電解液を破
棄することなく電解液を再利用することが出来、亜鉛の
損失もなく、廃水処理にも負担がかからず、しかも原鉱
石をも選ばない簡単なフッ素イオン除去方法が得られ、
また、硫酸チタニル・2水塩の添加によるもTiによる
汚染も生じない。
According to the present invention as described above, titanyl sulfate · 2 is contained in a zinc electrolyte having a high fluorine ion concentration.
By adding water salt, fluorine ions can be adsorbed and removed from the hydrolysis product, so that the electrolyte can be reused without discarding the electrolyte, without loss of zinc, and for wastewater treatment. A simple method for removing fluoride ions that does not require any burden and that does not select any ore,
Also, contamination by Ti does not occur even by the addition of titanyl sulfate dihydrate.

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 亜鉛電解液中に硫酸チタニル・2水塩を
添加し、アルカリpH調整剤を加えて加水分解生成物を
生成させ、電解液中のフッ素イオンを吸着除去させるこ
とを特徴とする亜鉛電解液中のフッ素イオン除去方法。
1. A method in which titanyl sulfate dihydrate is added to a zinc electrolytic solution, an alkaline pH adjuster is added to generate a hydrolysis product, and fluorine ions in the electrolytic solution are adsorbed and removed. Method for removing fluorine ions from zinc electrolyte.
【請求項2】 アルカリ調整剤によりpHを2.1〜
4.2の範囲に調整する請求項1記載の方法。
2. The pH is adjusted to 2.1 to 2.1 with an alkali adjuster.
4. The method of claim 1 wherein the adjustment is in the range of 4.2.
JP23898692A 1992-08-14 1992-08-14 Method for removing fluorine ions from zinc electrolyte Expired - Fee Related JP3144906B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP23898692A JP3144906B2 (en) 1992-08-14 1992-08-14 Method for removing fluorine ions from zinc electrolyte

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP23898692A JP3144906B2 (en) 1992-08-14 1992-08-14 Method for removing fluorine ions from zinc electrolyte

Publications (2)

Publication Number Publication Date
JPH0657476A JPH0657476A (en) 1994-03-01
JP3144906B2 true JP3144906B2 (en) 2001-03-12

Family

ID=17038230

Family Applications (1)

Application Number Title Priority Date Filing Date
JP23898692A Expired - Fee Related JP3144906B2 (en) 1992-08-14 1992-08-14 Method for removing fluorine ions from zinc electrolyte

Country Status (1)

Country Link
JP (1) JP3144906B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6143446A (en) * 1998-10-21 2000-11-07 Duracell Inc. Battery cathode
JP4907985B2 (en) * 2005-12-27 2012-04-04 三井金属鉱業株式会社 Fluorine removal method
JP4716913B2 (en) * 2006-04-05 2011-07-06 東北交易株式会社 Recycling of used titanium compounds as fluorine scavengers

Also Published As

Publication number Publication date
JPH0657476A (en) 1994-03-01

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