JP2000107525A - Method for cleaning filter of copper electrolyte filter device - Google Patents

Method for cleaning filter of copper electrolyte filter device

Info

Publication number
JP2000107525A
JP2000107525A JP10279084A JP27908498A JP2000107525A JP 2000107525 A JP2000107525 A JP 2000107525A JP 10279084 A JP10279084 A JP 10279084A JP 27908498 A JP27908498 A JP 27908498A JP 2000107525 A JP2000107525 A JP 2000107525A
Authority
JP
Japan
Prior art keywords
filter
filtration device
electrolytic
cleaning
water
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
JP10279084A
Other languages
Japanese (ja)
Inventor
Tsuneo Maruyama
恒夫 丸山
Takaharu Onizuka
隆治 鬼塚
Kenji Haisei
憲治 拝生
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 JP10279084A priority Critical patent/JP2000107525A/en
Publication of JP2000107525A publication Critical patent/JP2000107525A/en
Pending 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

  • Filtration Of Liquid (AREA)
  • Electrolytic Production Of Metals (AREA)

Abstract

PROBLEM TO BE SOLVED: To dispense with the use of a noxious hydrofluoric acid and thereby enhance the safety of a cleaning operation by cleaning a precoat-type filter which is clogged by a scale or a slime resulting from copper electrolysis, using an ultrasonic wave, when a suspended matter contained in an electrolyte is filtered with the help of a silica precoating agent. SOLUTION: A filter frame with a stainless steel woven metal wire is attached to the internal forward/backward faces of a filter device 3. A silica precoating agent layer is formed on each of the outside faces of the stainless steel woven metal wire using the self-circulation route of the filter device 3 and thus a precoat-type filter 4 is manufactured. When the precoat-type filter 4 which is useless due to clogging is cleaned, no noxious hydrofluoric acid is used. Consequently, a clog-causing matter is shaken to be loosened by suspending a plurality of ultrasonic oscillators 5 instead, in the water between the wall of a water tank and a soaked filter body. Alternatively, the ultrasonic oscillator 5 is attached to the filter device 3 to apply an ultrasonic oscillation to the filter body to loosen the clog-causing matter apart.

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は電気銅を製造する電
解精製法において、電解液中の浮遊物を除去する銅電解
液濾過装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a copper electrolytic solution filtering apparatus for removing suspended matter in an electrolytic solution in an electrolytic refining method for producing electrolytic copper.

【0002】[0002]

【従来の技術】銅の電解精製において用いられる電解液
は、その組成は銅35〜50g/l、硫酸140〜200g/lであり、
約20〜40l/min/槽の速度で電解槽に供給されている。電
解槽から溢流して出てきたこの電解液は濾過装置で浮遊
物を除去した後、循環槽に送られ、ここで陰極表面を平
滑にするための添加剤を加え、銅濃度および硫酸濃度を
調整し、次いで熱交換器で所定の液温にした後に、電解
槽に送り返され循環している。この浮遊物は主に微細な
スライムであり、導電性があるものもあるので、この浮
遊物を濾過装置で除去した後に電解槽に送り返さない
と、この浮遊物が陰極表面に付着して核となり、この核
を中心として銅が陰極板に電着・成長するので陰極表面
に突起物が形成されることになる。この突起物が大きく
成長し過ぎると陽極と接触してショートを起こし、操業
に支障を及ぼすだけでなく、この突起物は不純物を含ん
でいるので電気銅の純度低下の原因ともなる。
2. Description of the Related Art An electrolytic solution used in electrolytic refining of copper has a composition of 35 to 50 g / l of copper and 140 to 200 g / l of sulfuric acid.
It is supplied to the electrolytic cell at a rate of about 20-40 l / min / cell. The electrolytic solution that overflowed from the electrolytic cell was sent to a circulation tank after removing suspended matter by a filtration device, where an additive for smoothing the cathode surface was added, and the copper concentration and sulfuric acid concentration were reduced. After being adjusted and then brought to a predetermined liquid temperature by a heat exchanger, it is sent back to the electrolytic cell and circulated. This suspended matter is mainly fine slime, and there are some that have conductivity.If this suspended matter is not returned to the electrolytic cell after being removed by a filtration device, the suspended matter adheres to the cathode surface and becomes a nucleus. Since copper is electrodeposited and grown on the cathode plate around the nucleus, projections are formed on the cathode surface. If the projections grow too large, they will come into contact with the anode to cause a short circuit, which will not only hinder the operation, but also cause the purity of electrolytic copper to be reduced because the projections contain impurities.

【0003】この循環電解液の濾過には通常プレコート
式のフィルターが使用されている。これは布もしくはス
テンレス製金網の上に珪藻土その他のシリカ系プレコー
ト剤をコーティングして使用するフィルターである。こ
のプレコート式フィルターは10〜15日間通液するとプレ
コート層に捕捉した浮遊物の目詰まりにより通液抵抗が
高くなるので、濾過装置を止めて、プレコート層の再生
を行う。この再生は濾過装置内に設置してある水シャワ
ーにより目詰まりしたプレコート層を洗い落し、次いで
濾過装置の持つ自己循環経路を使用して再び布もしくは
ステンレス製金網の上に新しく珪藻土その他のシリカ系
プレコート剤をコーティングするものである。コーティ
ング後、再び電解液を通液して濾過している。
[0003] A pre-coated filter is usually used for filtering the circulating electrolyte. This is a filter that uses a diatomaceous earth or other silica-based precoat agent coated on a cloth or a stainless steel wire mesh. When the precoat filter is passed for 10 to 15 days, the flow resistance increases due to clogging of suspended matter trapped in the precoat layer. Therefore, the filtration device is stopped and the precoat layer is regenerated. In this regeneration, the clogged pre-coat layer is washed off by a water shower installed in the filtration device, and then the diatomaceous earth or other silica-based material is again placed on a cloth or a stainless steel wire mesh using the self-circulation path of the filtration device. This is to coat a precoat agent. After coating, the electrolyte solution is passed again and filtered.

【0004】しかしながら約6ヶ月間操業すると、布も
しくはステンレス製金網自体の目開きの部分にスケール
とプレコート材と微細なスライムからなる目詰まり物が
詰まって取れなくなり、洗浄・再プレコート剤コーティ
ングをしても通液抵抗が下がらず濾過不能となる。ここ
にいうスケールとは、砒素、アンチモン、カルシウム等
の電解液中からの析出物をいう。
[0004] However, after about 6 months of operation, the clogging material consisting of the scale, the precoat material and the fine slime is clogged in the openings of the cloth or the stainless steel wire mesh itself, and cannot be removed. Even though, the liquid flow resistance does not decrease and filtration becomes impossible. The term "scale" as used herein refers to a precipitate of arsenic, antimony, calcium, or the like from an electrolytic solution.

【0005】このため従来は濾過不能となった大きく重
量のあるフィルターを濾過装置から装置外に取り外し
て、まずプレコート層表面に付着している濾過された浮
遊物およびシリカ系プレコート剤を1平方センチメート
ル当たり100kgf以上の圧力を持つ高圧水でおおまかに除
去し(以後、前洗浄と呼ぶ)、次いでシリカ系プレコート
剤を溶解するのに一般的に使用されているフッ酸を満た
したフッ酸洗浄槽に40〜50分間浸漬してシリカ系プレコ
ート剤やスケールを溶解除去していた。そしてフッ酸洗
浄の終わった布もしくはステンレス製金網本体はフッ酸
洗浄槽より取り出して隣接する水槽でフッ酸を洗い流
し、フッ酸洗浄で溶解出来ずに残ったスケール等は1平
方センチメートル当たり100kgf以上の圧力を持つ高圧水
を使って吹き飛ばして除去・水洗していた。目詰まりを
解消した布もしくはステンレス製金網本体は再び濾過装
置内に戻し、濾過装置の持つ自己循環経路を使ってシリ
カ系プレコート層をその上に形成して、フィルターとし
て繰り返し使用していた。
[0005] Therefore, a large and heavy filter which cannot be filtered conventionally is removed from the filtering device to remove the suspended matter and the silica-based precoating agent adhering to the surface of the precoat layer per square centimeter. It is roughly removed with high-pressure water having a pressure of 100 kgf or more (hereinafter referred to as pre-cleaning), and then placed in a hydrofluoric acid cleaning tank filled with hydrofluoric acid which is generally used to dissolve a silica-based precoat agent. The silica-based precoat agent and scale were dissolved and removed by immersion for ~ 50 minutes. The hydrofluoric acid-washed cloth or stainless steel wire mesh body is removed from the hydrofluoric acid cleaning tank, and the hydrofluoric acid is rinsed off in the adjacent water tank.The remaining scale, etc. that could not be dissolved by hydrofluoric acid cleaning was over 100 kgf per square centimeter It was blown off using high-pressure water with water and removed and washed. The cloth or the stainless steel wire mesh body from which the clogging was eliminated was returned to the filtration device again, and the silica-based precoat layer was formed thereon using the self-circulation path of the filtration device, and was repeatedly used as a filter.

【0006】なお、フッ酸はフッ化水素酸とも呼ばれフ
ッ化水素の水溶液である。フッ化水素はその水溶液とと
もに極めて毒性が強く、皮膚に触れると激しく痛み、内
部に浸透して細胞を腐食する。フッ酸の代わりに希塩酸
を使うと特にステンレス製金網の場合にはステンレス材
が腐食されてしまうので好まれない。
[0006] Hydrofluoric acid is also called hydrofluoric acid and is an aqueous solution of hydrogen fluoride. Hydrogen fluoride, along with its aqueous solution, is extremely toxic; it is severely painful when it comes in contact with the skin and penetrates inside and corrodes cells. It is not preferable to use dilute hydrochloric acid instead of hydrofluoric acid, particularly in the case of a stainless steel wire mesh because the stainless steel material is corroded.

【0007】[0007]

【発明が解決しようとする課題】シリカ系プレコート層
を溶解するフッ酸は弱酸であるが上述のように毒性が強
い。このフッ酸を満たしたフッ酸洗浄槽に、大きく重量
のあるフィルターを出し入れする作業はフッ酸の飛び散
り等、安全上問題があった。
The hydrofluoric acid that dissolves the silica-based precoat layer is a weak acid, but has high toxicity as described above. The operation of putting a large and heavy filter into and out of the hydrofluoric acid cleaning tank filled with hydrofluoric acid has safety problems such as scattering of hydrofluoric acid.

【0008】さらに、フッ酸の入った洗浄槽から取り出
した布もしくはステンレス製金網には、完全に溶解でき
なかったプレコート剤とスケールとが部分的に残留して
おり、水洗用水槽でフッ酸を洗い流した後、これらは1
平方センチメートル当たり100kgf以上の高圧洗浄水を用
いて吹き飛ばして洗い流していたが、この高圧洗浄水が
布もしくはステンレス製金網に当たった際に、作業員の
顔面に跳ね返ってきたり、あるいはまわりに飛び散って
危険であった。
Further, the cloth or stainless steel wire mesh removed from the washing tank containing hydrofluoric acid partially retains the precoating agent and the scale which could not be completely dissolved, and the hydrofluoric acid was removed in the washing water tank. After washing, these
It was blown off using high-pressure washing water of 100 kgf or more per square centimeter and was washed off.However, when this high-pressure washing water hit a cloth or a stainless steel wire mesh, it bounced off the worker's face or scattered around and was dangerous. there were.

【0009】また、このようなフッ酸を使った洗浄作業
を行うのに、例えば濾過装置から36枚のフィルターを取
り外す場合、フィルターの取り外しに二人作業で約4時
間、前洗浄に40分/枚x36枚=約24時間(一人作業)、フッ
酸洗浄に二人作業で約2時間、スケール等除去のための
高圧水洗浄に前洗浄と同じ約24時間(一人作業)、洗浄の
終わったフィルターの取り付けに二人作業で約4時間、
合計約58時間(うち二人作業は約10時間)という時間と労
力を費やしていた。
In addition, when performing such a cleaning operation using hydrofluoric acid, for example, when 36 filters are removed from the filtration device, it takes about 4 hours to remove the filters by two persons, and 40 minutes per pre-cleaning. Sheet x 36 = about 24 hours (one person work), cleaning with hydrofluoric acid about 2 hours with two people work, washing with high pressure water for scale removal about the same about 24 hours as the previous wash (one person work), cleaning was completed It takes about 4 hours for two people to install the filter,
A total of about 58 hours (including about 10 hours for two-person work) were spent.

【0010】このため、銅電解用の循環電解液の濾過装
置において、目詰まりを起こしたプレコート式フィルタ
ーを、安全簡単に洗浄する方法が求められていた。
[0010] Therefore, there has been a demand for a method for safely and easily cleaning a pre-coated filter having clogged in a circulating electrolytic solution filtering device for copper electrolysis.

【0011】[0011]

【課題を解決するための手段】本発明は上記の問題を解
決するため、電解槽から電解液を溢流させて抜き出し、
電解液中の浮遊物を濾過装置にて濾過後、該濾液を電解
槽に返流循環する銅の電解精製法における銅電解液濾過
装置のフィルター洗浄方法において、前記濾過装置から
目詰まりして通液が困難となったフィルターを取り出
し、前記フィルターを外周もしくは内部に超音波発振器
を設置してある水槽の水中に浸漬し、または水槽の水中
に浸漬後、水槽の外周もしくは内部に超音波発振器を設
置し、超音波振動を前記フィルターに加えて、前記フィ
ルターの目詰まり物の固着を弛緩させ、弛緩した前記目
詰まり物を高圧水で吹き飛ばして洗浄した後、このプレ
コート式フィルターを再び濾過装置の中に戻して再使用
することを特徴とする、銅電解液濾過装置のフィルター
洗浄方法である。
SUMMARY OF THE INVENTION The present invention solves the above-mentioned problems by overflowing and extracting an electrolytic solution from an electrolytic cell.
After the suspended matter in the electrolytic solution is filtered by a filtration device, the filtrate is returned and circulated to an electrolytic tank. In the filter cleaning method of the copper electrolyte filtration device in the electrolytic copper purification method, the filtration device is clogged and passed. Take out the filter in which the liquid became difficult, immerse the filter in the water of the water tank in which the ultrasonic oscillator is installed on the outer circumference or inside, or after immersing in the water of the water tank, put the ultrasonic oscillator on the outer circumference or inside the water tank. After installing, applying ultrasonic vibration to the filter to loosen the adhesion of the clogging of the filter, washing the loosened clogging by blowing it off with high-pressure water, the pre-coated filter is again filtered by the filtration device. A filter cleaning method for a copper electrolyte solution filtration device, wherein the filter is returned to the inside and reused.

【0012】また、目詰まりを起こしたプレコート式フ
ィルターを、さらに安全に簡単に洗浄するために、濾過
装置本体の外周もしくは内部に超音波発振器を設置して
ある濾過装置に、目詰まりしたプレコ−ト式フィルタ−
を取り付けたまま洗浄するにあたり、洗浄中に超音波振
動を加えて、前記フィルターの目詰まり物の固着を弛緩
させ、弛緩した前記目詰まり物を濾過装置内に設置して
ある水シャワーにより洗い流して洗浄することを特徴と
する、銅電解液濾過装置のフィルター洗浄方法である。
Further, in order to further safely and easily clean the clogged pre-coated filter, the clogged pre-coated filter is installed in a filtration device having an ultrasonic oscillator installed on the outer periphery or inside of the filtration device main body. G filter
When washing with the filter attached, ultrasonic vibration is applied during the washing to loosen the fixation of the clogging material of the filter, and the loosened clogging material is washed away by a water shower installed in a filtration device. A filter cleaning method for a copper electrolyte solution filtration device, characterized by performing cleaning.

【0013】[0013]

【発明の実施の形態】まず、一例としてステンレス製金
網1の上にプレコ−ト層を形成する方法について簡単に
述べる。濾過装置3の中に、図2に示すように前後面に
それぞれ2面、合計4面のステンレス製金網1を持つフ
ィルター枠2を所定の枚数、例えば36枚取り付ける。濾
過装置3の持つ自己循環経路を使ってシリカ系プレコー
ト剤、例えば珪藻土の層をそのステンレス製金網の各外
側面上に形成して、プレコート式フィルター4は出来上
がる。その大きさは縦約900mm、横約1800mm、厚み約30m
mである。なお、ステンレス製金網の内側部分は濾液の
通り道となる。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS First, a method of forming a precoat layer on a stainless steel wire net 1 will be briefly described as an example. As shown in FIG. 2, a predetermined number of filter frames 2 having a total of four stainless steel wire nets 1, for example, 36, are mounted in the filtration device 3 as shown in FIG. A layer of a silica-based precoat agent, for example, diatomaceous earth, is formed on each outer surface of the stainless steel wire mesh using the self-circulation path of the filtration device 3, and the precoat-type filter 4 is completed. The size is about 900mm in length, about 1800mm in width, about 30m in thickness
m. The inside of the stainless steel wire mesh is a passage for the filtrate.

【0014】この珪藻土をプレコートしたフィルターに
硫酸酸性の硫酸銅の電解液を通し、浮遊物を濾過した。
通液抵抗上昇に伴い10〜15日毎に濾過装置の運転を止め
てのプレコート層の再生、すなわち前述したようなシリ
カ系プレコート層の張替えを繰り返しながら循環電解液
を濾過していたが、約6ヶ月後に目詰まりにより、プレ
コート層を再生しても通液能力回復が困難となった。
A sulfuric acid electrolytic solution of copper sulfate was passed through the filter precoated with diatomaceous earth to filter the suspended matter.
Regeneration of the precoat layer by stopping the operation of the filtration device every 10 to 15 days due to an increase in liquid flow resistance, that is, the circulating electrolyte was filtered while repeating the recoating of the silica-based precoat layer as described above. Clogging after one month made it difficult to recover the liquid permeation ability even if the precoat layer was regenerated.

【0015】第1の発明は、目詰まりを起こして使用不
能になったプレコート式フィルターの洗浄に有毒のフッ
酸を使わない方法である。第1発明の実施例として、濾
過装置から取り出した目詰まりのあるステンレス金網製
フィルターは、まず1平方センチメートル当たり100kgf
以上の高圧水を用いて、珪藻土からなるプレコート層表
面に付着している主成分がスライムである黒い浮遊物を
吹き飛ばすとともに、できるだけ珪藻土の層を除去す
る。ついでこれらフィルター本体を12枚、ハンガーで吊
り上げ、1.7立方メートルの水槽の水中に完全に浸漬し
た。
The first invention is a method in which toxic hydrofluoric acid is not used for cleaning a precoated filter that has become unusable due to clogging. As an embodiment of the first invention, a clogged stainless steel wire mesh filter taken out of a filtration device is first supplied with 100 kgf per square centimeter.
Using the above high-pressure water, the black suspended matter whose main component is slime, which is attached to the surface of the pre-coat layer made of diatomaceous earth, is blown off, and the diatomaceous earth layer is removed as much as possible. Next, 12 of these filter bodies were lifted with a hanger and completely immersed in water of a 1.7 cubic meter water tank.

【0016】この水槽壁と浸漬したフィルター本体との
間の水中に6個、超音波発振器を吊り下げ、30〜60分間
発振して目詰まり物の固着を弛緩させた。この超音波洗
浄を終えたステンレス金網製フィルター本体には弛緩し
た目詰まり物であるスケールや固くなったプレコート剤
等が付着しているので、水槽から取り出した後、1平方
センチメートル当たり100kgf以上の高圧水を用いてこれ
ら弛緩した目詰まり物を吹き飛ばす。
Six ultrasonic oscillators were suspended in water between the water tank wall and the immersed filter body, and oscillated for 30 to 60 minutes to loosen the fixation of the clogged material. After the ultrasonic cleaning, the stainless steel wire mesh filter body contains loose clogging scales and hardened pre-coating agent.After removing from the water tank, high pressure water of 100 kgf or more per square centimeter Blow away these loose clogs.

【0017】このようにして洗浄の終了したステンレス
金網製フィルター本体を濾過装置3に戻し、前述した通
常の方法によりシリカ系プレコート剤をコーティング
後、循環電解液を通液したところ、問題なく通液するこ
とができた。
The filter body made of the stainless steel wire mesh which has been washed as described above is returned to the filtration device 3 and coated with a silica-based pre-coating agent by the above-mentioned ordinary method. We were able to.

【0018】第2の発明は、有毒なフッ酸も高圧水も使
わず、しかも上述した第1の発明のような濾過装置3か
らの面倒なプレコート式フィルター4の取り外し・取り
付け、および水槽での洗浄が不要になる方法である。
The second invention uses neither toxic hydrofluoric acid nor high-pressure water, and also has the troublesome removal and installation of the pre-coated filter 4 from the filtration device 3 as in the above-described first invention, and the use of a water tank. This method eliminates the need for cleaning.

【0019】第2の発明の実施例として、濾過装置3に
図1に示すように超音波発振器5を取り付ける。通液抵
抗上昇に伴い10〜15日毎に濾過装置を止めて、目詰まり
したプレコート層を除去した後、濾過装置内に水を張り
込み、超音波振動がフィルターに加わるようにして超音
波洗浄を毎回60分間実施した。これによりスケールの固
着が大きく成長しないうちに、またシリカ系プレコート
剤の固着が軽度のうちに、ステンレス製金網の目詰まり
物を弛緩させ、この弛緩した目詰まり物を濾過装置内に
設置してある水シャワーにより表面のプレコート層とと
もに洗い流して洗浄する。
As an embodiment of the second invention, an ultrasonic oscillator 5 is attached to the filtering device 3 as shown in FIG. Stop the filtration device every 10 to 15 days due to the increase in liquid flow resistance, remove the clogged pre-coat layer, fill the water into the filtration device, apply ultrasonic vibration to the filter, and perform ultrasonic cleaning every time. Performed for 60 minutes. As a result, the clogging of the stainless steel wire gauze is relaxed before the adhesion of the scale does not grow significantly and the adhesion of the silica-based precoat agent is mild, and the loose clogging is set in the filtration device. It is washed off with a pre-coat layer on the surface by a certain water shower.

【0020】この方法により、洗浄効率が格段に向上
し、フィルターの目詰まりによりプレコート層を再生し
ても通液能力回復ができなくなる間隔が6ヶ月から1年6
ヶ月に延びた。これにより、プレコート式フィルターを
濾過装置外に取り出して洗浄するに要する時間(フィル
ター枚数36枚の場合、1回当たり約58時間)とそれに費
やす労力が節減できた。
According to this method, the washing efficiency is remarkably improved, and the interval at which the passage capacity cannot be recovered even when the precoat layer is regenerated due to clogging of the filter is from 6 months to 1 year.
Extended to months. As a result, the time required to take out the pre-coated filter out of the filtration device and to wash it (about 58 hours per time for 36 filters) and the labor required for it can be reduced.

【0021】[0021]

【発明の効果】以上説明したように、硫酸酸性の硫酸銅
溶液である電解液中の浮遊物をシリカ系プレコート剤を
用いて濾過するプレコ−ト式フィルターの洗浄方法にお
いて、銅電解に起因するスケールやスライムによって発
生する目詰まりのあるプレコ−ト式フィルタ−を超音波
洗浄することにより、 第一の発明では、洗浄に有毒の
フッ酸を使わなくて済むようになり作業の安全性が格段
に向上した。
As described above, in the method for cleaning a precoat filter in which suspended matter in an electrolytic solution, which is a sulfuric acid-acidic copper sulfate solution, is filtered using a silica-based precoating agent, the method is based on copper electrolysis. By ultrasonically cleaning the pre-coated filter with clogging caused by scale and slime, the first invention makes it unnecessary to use toxic hydrofluoric acid for cleaning, thus greatly improving the safety of work. Improved.

【0022】また第2の発明では、有毒なフッ酸に加え
て危険な高圧洗浄水も使わなくて済み、しかも面倒な濾
過装置からのフィルターの取り外し・取り付け、ならび
に水槽での洗浄作業回数が減少した。
According to the second aspect of the present invention, in addition to toxic hydrofluoric acid, dangerous high-pressure washing water is not required, and the troublesome removal and installation of the filter from the filtration device and the number of washing operations in the water tank are reduced. did.

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

【図1】超音波発振器を取り付けた、プレコート式フィ
ルターを用いる濾過装置の概略図
FIG. 1 is a schematic diagram of a filtration device using a pre-coated filter equipped with an ultrasonic oscillator.

【図2】シリカ系プレコート層をその上に形成する前の
ステンレス製金網を示す概略図
FIG. 2 is a schematic view showing a stainless steel wire mesh before a silica-based precoat layer is formed thereon.

【符号の説明】[Explanation of symbols]

1 ステンレス製金網 2 フィルター枠 3 濾過装置 4 プレコート式フィルター 5 超音波発振器 6 循環電解液入口配管 7 フィルターの濾液出口 8 濾液配管 9 濾液出口配管 10 蓋 A 濾過前の循環電解液 B 循環電解液の濾液 DESCRIPTION OF SYMBOLS 1 Stainless steel wire mesh 2 Filter frame 3 Filtration device 4 Precoat type filter 5 Ultrasonic oscillator 6 Circulating electrolyte inlet pipe 7 Filter filtrate outlet 8 Filtrate pipe 9 Filtrate outlet pipe 10 Lid A Circulating electrolyte before filtration B Circulating electrolyte Filtrate

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 電解槽から電解液を溢流させて抜き出
し、電解液中の浮遊物を濾過装置にて濾過後、該濾液を
電解槽に返流循環する銅の電解精製法における銅電解液
濾過装置のフィルター洗浄方法において、前記濾過装置
から目詰まりして通液が困難となったフィルターを取り
出し、前記フィルターを外周もしくは内部に超音波発振
器を設置してある水槽の水中に浸漬し、または水槽の水
中に浸漬後、水槽の外周もしくは内部に超音波発振器を
設置し、超音波振動を前記フィルターに加えて、前記フ
ィルターの目詰まり物の固着を弛緩させ、弛緩した前記
目詰まり物を高圧水で吹き飛ばして洗浄した後、このプ
レコート式フィルターを再び濾過装置の中に戻して再使
用することを特徴とする、銅電解液濾過装置のフィルタ
ー洗浄方法。
1. A copper electrolytic solution in an electrolytic copper refining method in which an electrolytic solution overflows from an electrolytic bath and is withdrawn, a suspended matter in the electrolytic solution is filtered by a filtration device, and the filtrate is returned and circulated to the electrolytic bath. In the filter cleaning method of the filtration device, take out the filter that has become difficult to pass through the clogged filter from the filtration device, immersed the filter in the water of the water tank where an ultrasonic oscillator is installed on the outer periphery or inside, or After immersion in the water in the water tank, an ultrasonic oscillator is installed on the outer periphery or inside of the water tank, and ultrasonic vibration is applied to the filter to loosen the clogging of the filter, and the loosened clogging is performed at a high pressure. A method for cleaning a filter for a copper electrolyte filtration device, comprising washing the pre-coated filter again by blowing it off with water, and then returning the precoated filter to the filtration device for reuse.
【請求項2】 電解槽から電解液を溢流させて抜き出
し、電解液中の浮遊物を濾過装置にて濾過後、該濾液を
電解槽に返流循環する銅の電解精製法における銅電解液
濾過装置のフィルター洗浄方法において、前記濾過装置
本体の外周もしくは内部に超音波発振器を設置してある
濾過装置に、目詰まりしたプレコ−ト式フィルタ−を取
り付けたまま洗浄するにあたり、洗浄中に超音波振動を
加えて、前記フィルターの目詰まり物の固着を弛緩さ
せ、弛緩した前記目詰まり物を濾過装置内に設置してあ
る水シャワーにより洗い流して洗浄することを特徴とす
る、銅電解液濾過装置のフィルター洗浄方法。
2. A copper electrolytic solution in an electrolytic copper refining method in which an electrolytic solution overflows from an electrolytic cell and is withdrawn, a suspended matter in the electrolytic solution is filtered by a filtration device, and the filtrate is returned and circulated to the electrolytic cell. In the method of cleaning a filter of a filtration device, when a clogged pre-coat type filter is mounted on a filtration device having an ultrasonic oscillator installed on the outer periphery or inside of the filtration device main body, an ultra-fine Applying a sonic vibration to loosen the fixation of the clogging material of the filter, and washing the loosened clogging material with a water shower installed in a filtration device to wash the copper electrolyte solution. How to clean the filter of the device.
JP10279084A 1998-09-30 1998-09-30 Method for cleaning filter of copper electrolyte filter device Pending JP2000107525A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10279084A JP2000107525A (en) 1998-09-30 1998-09-30 Method for cleaning filter of copper electrolyte filter device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10279084A JP2000107525A (en) 1998-09-30 1998-09-30 Method for cleaning filter of copper electrolyte filter device

Publications (1)

Publication Number Publication Date
JP2000107525A true JP2000107525A (en) 2000-04-18

Family

ID=17606202

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10279084A Pending JP2000107525A (en) 1998-09-30 1998-09-30 Method for cleaning filter of copper electrolyte filter device

Country Status (1)

Country Link
JP (1) JP2000107525A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001087459A1 (en) * 2000-05-18 2001-11-22 Mitsui Mining & Smelting Co.,Ltd. Method for filtration of copper electrolyte solution
JP2005211703A (en) * 2004-01-27 2005-08-11 Okumura Corp Filtering method
CN102350140A (en) * 2011-08-01 2012-02-15 山西太钢不锈钢股份有限公司 Method for cleaning filter core of filter
CN106011930A (en) * 2016-07-28 2016-10-12 河南豫光金铅股份有限公司 Continuous preparation method of refining electrolytic solution for copper electrolysis
CN110624315A (en) * 2019-02-24 2019-12-31 田大志 Environment-friendly treatment method for recycling polluted and ineffective filter material
CN114536202A (en) * 2022-01-08 2022-05-27 浙江福达合金材料科技有限公司 Novel surface treatment method for copper contact bridge
CN114653138A (en) * 2022-02-25 2022-06-24 中信重工机械股份有限公司 Horizontal suspension type ultrasonic cleaning device of disc filter

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001087459A1 (en) * 2000-05-18 2001-11-22 Mitsui Mining & Smelting Co.,Ltd. Method for filtration of copper electrolyte solution
JP2005211703A (en) * 2004-01-27 2005-08-11 Okumura Corp Filtering method
CN102350140A (en) * 2011-08-01 2012-02-15 山西太钢不锈钢股份有限公司 Method for cleaning filter core of filter
CN106011930A (en) * 2016-07-28 2016-10-12 河南豫光金铅股份有限公司 Continuous preparation method of refining electrolytic solution for copper electrolysis
CN106011930B (en) * 2016-07-28 2018-09-25 河南豫光金铅股份有限公司 A kind of continuous preparation method of cupric electrolysis refining electrolyte
CN110624315A (en) * 2019-02-24 2019-12-31 田大志 Environment-friendly treatment method for recycling polluted and ineffective filter material
CN114536202A (en) * 2022-01-08 2022-05-27 浙江福达合金材料科技有限公司 Novel surface treatment method for copper contact bridge
CN114653138A (en) * 2022-02-25 2022-06-24 中信重工机械股份有限公司 Horizontal suspension type ultrasonic cleaning device of disc filter
CN114653138B (en) * 2022-02-25 2023-02-28 中信重工机械股份有限公司 Horizontal suspension type ultrasonic cleaning device of disc filter

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