JPS60234989A - Electrodeposition cell of waste liquid containing metallic ion - Google Patents

Electrodeposition cell of waste liquid containing metallic ion

Info

Publication number
JPS60234989A
JPS60234989A JP9036984A JP9036984A JPS60234989A JP S60234989 A JPS60234989 A JP S60234989A JP 9036984 A JP9036984 A JP 9036984A JP 9036984 A JP9036984 A JP 9036984A JP S60234989 A JPS60234989 A JP S60234989A
Authority
JP
Japan
Prior art keywords
cell
waste liquid
metals
deposited
electrodeposition
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.)
Granted
Application number
JP9036984A
Other languages
Japanese (ja)
Other versions
JPS6312153B2 (en
Inventor
Tatsuya Uchida
達也 内田
Yuji Shinoda
篠田 勇治
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.)
Resonac Corp
Original Assignee
Hitachi Chemical 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 Hitachi Chemical Co Ltd filed Critical Hitachi Chemical Co Ltd
Priority to JP9036984A priority Critical patent/JPS60234989A/en
Publication of JPS60234989A publication Critical patent/JPS60234989A/en
Publication of JPS6312153B2 publication Critical patent/JPS6312153B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To deposit and recover metals from waste liquid with excellent power efficiency by separating a cell with a partition wall into a cell provided with many electrodes and a cell wherein waste liquid is pumped up, and circulating waste liquid rapidly through both cells when metals dissolved in industrial waste liquid from plating, etc. are deposited and recovered. CONSTITUTION:Metals in waste liquid discharged from a plating factory, etc. and contg. metals are deposited in an electrodeposition cell to remove and recover the metals. In this case, the electrodeposition cell 1 is separated with a partition wall 2 into a pumped cell 4 and a cell 6 provided with a group of electrodes. and both cells are communicated at the bottom part. A gas such as air is bubbled out from a diffuser pipe 3 for air lifting provided in the pumped cell 4, and waste liquid is sent upward by the bubbles and flown over the partition wall 2 into the cell 6 provided with a group of electrodes. A group of electrodes consisting of many anodes 5a and cathodes 5b are provided in the cell 6. Metallic ions in waste liquid are deposited on the reticular cathode 5n, dropped, and accumulated at the bottom of the electrodeposited cell 1 as electrodeposited metals 8. The circulation of waste liquid through both cells 4 and 6 is accelerated, and the dissolved metals are deposited and removed with high power efficiency.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明rr産lN溌猷特にメッキエ東廃猷等に^1m1
度に含有され/)蛸、鉛、ニツクル、クロム等の金M(
オン?f−電気的に除去する電屏析出情(以下電析憎と
いう)に関すゐ〇 〔従来技術〕 従来、メッキ工場等から排出される廃欣に宮まれる前記
金属1オンの除去装置やll2I収装置として純凝り^
い金J!I4粉や金属船か回収できる電析情か多く用い
られてきた0この方式τ用いて。
[Detailed description of the invention] [Industrial application field] The present invention can be applied to RR-produced lN lively water, especially Mekke Higashi-hai, etc.^1m1
Gold M (contained in degrees/), lead, nickel, chromium, etc.
on? f- Regarding electrolytic removal (hereinafter referred to as electrodeposition) [Prior art] Conventionally, the above-mentioned metal removal equipment and ll2I installed in waste discharged from plating factories, etc. Pure as a storage device ^
Ikin J! This method has been widely used for electrodeposition that can be recovered from I4 powder or metal vessels.

大賞り廃猷τ短時間で経済的に処理するにa竜極敬τ多
数密−に配設し史に電憔間ギョリτ極少に押えることか
必食であり1電力効率τ瑣刀Ωさぜゐ罠めの電析敵の償
件刀式τも塙慮した電析憎栴輩及び篭他孜配設法に格段
の工夫τ必資とし罠0又、電析に付随して発生する酸系
、累系カスの01燃、$1発性ガスや廃除中に塩素1オ
ン有機?7が甘lγLる場合に発生する腐食性の塩素ガ
ス%悪臭カスに対する人的、a憧的安全性の確保の問題
も考鳳しなければならない〇攪拌方式としてね、従来よ
り電極群り下部τ攪袢真により撹拌する方法やボン1に
よるaOa環及び−気にj6攪拌法等かあった。最も鮭
埼的な攪拌方式に、9!気にLる一気攪拌力式といわれ
るか狭い’[極間を気泡が上昇するため極間電圧が上昇
し電力費の増7111VCつながる欠点があった。ま7
c危険で不快な発生ガス処理Kに、電析僧を略密閉式と
して21ン等で吸引しガス処理r行っているか処理に用
いられる機器の防爆性、耐食性に必*以上の設備を設け
なけnばならなかっ友〇 〔発明の目的〕 不発明に電析惰内欣のi件と電極群配役の改良を行い電
力効率と安全性盆尚めることかできる寛析情を提供する
ことt目的とする。
In order to economically dispose of the waste in a short time, it is necessary to arrange it in large numbers densely and to minimize the electric power efficiency.ゐThe electrodeposition enemy's redemption method τ has also been taken into account, and the method of setting the electrodeposition has been significantly devised. , 01 combustion of cumulative scum, $1 gas and 1 chlorine 1 organic during waste removal? We must also take into consideration the issue of ensuring human and aspirational safety against the corrosive chlorine gas% foul-smelling scum that is generated when 7. There were methods of stirring with a stirrer, a method of aOa ring using a bong 1, and a method of stirring with an aOa ring using a bong 1. 9 for the most salmon-like stirring method! It is said to be a one-shot stirring force type, which has the drawback that air bubbles rise between the electrodes, which increases the voltage between the electrodes and increases electricity costs. Ma7
c To process the dangerous and unpleasant generated gases, whether the electrolytic metal is suctioned in a nearly closed system using a 21-ton gas treatment r, or the equipment used for the treatment must be equipped with the necessary equipment to ensure explosion-proof and corrosion-resistant properties. A must-have friend〇 [Object of the invention] To provide an easy-to-understand method that can improve power efficiency and safety by improving the internal conditions of electrodeposition and the arrangement of electrode groups. purpose.

〔発明の摘取〕[Invention extraction]

不発FiAに上端部に越流壜を倫えた隔壁に19槽を底
部を連通させて分画し、一槽を電析欣儂環用のエアーリ
スト用散気管を設けた揚水惜となし、他檜を仮数の電析
用電極板が越流堰に垂直かつ鉛直に配役さn、揚水され
た電析aが電極板間を流TTゐ′亀惚群配設惜となし、
僧低部に析出金属の業m部を設けたことt峙倣とする金
楓イオン含M廃敵の電析憎に関する。
The unexploded FiA was separated by connecting 19 tanks at the bottom to a bulkhead with an overflow bottle on the top end, and one tank was used as a pumping tank equipped with an aeration pipe for the air list for electrolytic deposition, etc. Electrode plates made of Japanese cypress are arranged vertically and perpendicularly to the overflow weir, and the pumped electrodeposition a flows between the electrode plates.
It is related to the electrodeposition of the gold maple ion-containing metal, which is imitated by the provision of a precipitated metal part in the lower part of the lower part.

以下不発明を図面に基いて説明する◎i1図a電析債の
鉤部断面図であり第2図は平向内である0#4斜妊st
もつ電析憎1a底部を連通させて上端部に越流堰を儒え
た隔壁2で分画さnている。分画した一僧にエアーリフ
ト用散気管5を設けycltiiX槽4とする。エアー
リント用気体に一般的にa空気5%株な場合には不活性
ガスを用いる。
The non-invention will be explained below based on the drawings. ◎I1 Figure a is a cross-sectional view of the hook part of the electrodeposited bond, and Figure 2 is the 0#4 oblique gravitational force in the horizontal direction.
The bottom part of the electrodeposition tube 1a is communicated with each other and separated by a partition wall 2 having an overflow weir at the top end. A diffuser tube 5 for air lift is provided to the fractionated tube to form a ycltiiX tank 4. Generally, when the air lint gas is 5% a-air, an inert gas is used.

分画し?C他檜にa、第2図に示すように越訛堰に対し
嵩直に77毒つ蛤直に電析用電極板5a。
Fractionation? As shown in FIG. 2, the electrode plate 5a for electrodeposition is placed directly on the cypress 77 and directly on the weir.

5br複数配設し電極群配設憎6と1丁。即ち揚水偕4
で揚水された電?raa越訛櫃τ越流し電&債6の[極
mrT!J*平行にかつ均等に電他僧紙部に同かって流
下した恢豊び隔壁2の1趨の連通部から揚水憎4へ上昇
し、循環を操り返すうちに電析にLり金輌イオンa隘他
5b上に金属として析出し処理されるものである。この
時。
5BR multiple arrangement, electrode group arrangement 6 and 1 unit. That is, pumping water 4
Electricity pumped from water? Raa Koshikashi τ Overflow Den & Bond 6 [Extreme mrT! J * In parallel and evenly, the metal ions flowed down from the connecting part of the bulkhead 2 to the pumping water 4, and as the circulation was reversed, L metal ions were deposited into the electrodeposit. The metal is precipitated on the a and other parts 5b. At this time.

揚水に用いらnた空気や不宿性ガスに1鋤水僧の水rk
Jか゛ら放出さnるπめ電極群間へ曵入することになく
、又電析にLる発生カス%−水tτ増すことKLU極間
を上昇する19%流れに乗って揚7X偕へ回遊し、揚水
憎から飛散するため電極間に存在する免停a微かとなり
他間電圧抵抗も最小となり電力費の低mにつながる0工
アーリフト用気体’kj’m刀0することで、僧門循環
回数が増力口し′醒析効米ひいてに電力効率の上昇と発
生ガスの放散、希釈、ガス処理装置への圧送KM効とな
る。しかし循環tgI数の増力口は、理論的に限界かあ
るので史に゛酸析幼果τpII加さぜるπめに01!他
板間を流ト丁ゐ亀解欣に更に強い攪拌を与えるため、電
億形状で金網状、バンチングメタル状、工千スパンダメ
タル状の多孔板とするのか望ましい0−力、このことに
、陰極板5b土に析出丁ゐ金楓形秋か箔状でになく粒状
治しく0411枝状となる幼果t%1ち、循環電析aK
Lr)億板上から容易に剥離し沈降する0電析僧底Sに
0傾斜した餞面を待つ析出金属果極myか設けらnてお
り、析出金顧のall励、弓1き抜きが容易となゐ0 史に菟析惜傅造として0第6図り如(第1図り電析検電
・2檜組み台ぜかつ中央隔壁りF部γ連逍して屯り丁並
#の梁槙郡τ兼用しに侑迫や粥4図の如くエアーリント
鍋水都τ情り中天hμに設ける慣這にしたもりか実用的
であゐO第5図に不発明との比較りπめ用い罠矩形篭併
情で内部り配設電悌硅a第1凶と全く1町株で篭惨軒下
部r、 り !惨群配収方向に散気室〃二設けπtりで
あゐ。
Add 1 plow water to the air and inhospitable gases used for pumping water.
The generated gas % - water tτ increases during electrodeposition without infiltrating between the electrode groups. However, since the water is scattered from the pumping water, the voltage resistance between the electrodes becomes slight, and the voltage resistance between the electrodes is also minimized, which leads to lower power costs. The number of times increases the power output, improves the clarification effect, increases the power efficiency, dissipates the generated gas, dilutes it, and pressure-feeds it to the gas processing equipment. However, since there is a theoretical limit to the increase in the number of circulating tgI, adding ``acidification infant τpII'' to the history is 01! In order to give even stronger agitation to the flow between the plates, it is desirable to use a perforated plate in the shape of wire mesh, bunching metal, or spanned metal. Cathode plate 5b Deposited on soil Gold maple-shaped fall, not foil-like but granular, 0411 Branch-like young fruit t%1, circulating electrodeposition aK
Lr) There is a precipitated metal pole on the deposited metal bottom S which easily peels off and settles from the plate, and there is a precipitated metal tip waiting for the tilted surface of the deposited metal. It is easy to understand that the 6th plan is as follows. It is practical to use the air lint pot Suito τ, as shown in Figure 4 of Yusako and Kayu, as shown in Fig. 4. In a rectangular trap, there are two internally installed electric cables, one at the bottom of the eaves, and two diffuser chambers in the direction of the group.

以下不発用」τ実施ν0比板例に基いて線切する。The following is a line cut based on the example of the τ implementation ν0 ratio plate for misfires.

〔実施例、比軟νす〕[Example, specific softness]

第1図と第5図c/)岨所憎τ用いて畝気窒気電τ10
」−にし、゛龜流雀腿、゛亀流嵌腿1 也訛電寺電析条
件τ全(同一にして次−1の懺ば納τ含むメッキ屏欲り
衣−2Q亀釘朱杆で酸析処理τ竹っπ精米τ第6図、衣
−3に示すO 表17ツキ廃猷(L)猷貴 表2嵐析朱汗 衣6 庄) 内資電析時間とa銅醸親か10 U@76になゐ
箇での時間とし7C。
Fig. 1 and Fig. 5 c/) Using the ridge temperature τ10
''-, then ``Kameryu Suzuki,'' ``Kameryu Matsuri 1 and Kandenji electrodeposition conditions τ all (same and the following -1 results τ including plating folding cloth - 2Q Tortoise nail red rod. Acid precipitation treatment τ Bamboo π rice polishing τ Figure 6, O shown in Cloth-3 10 U @ 76 and the time is 7C.

これらV結果に示す様に比較例a散気空気による篭導批
仇がλきいため電圧も尚く、更に撹(′l!効果が悪い
ので、鯖−厩が低凝眩にlゐに従い電析i@度か遅(な
ゐ。こnに比軟し不発明では電圧が低く平板陰惨で用い
ても比較例の3倍もの銅析出讐が侍られ、更に陰惨てパ
ンチングメタルQ)多孔機陰極τ用いると5倍も良好な
結果となっπ0まπこの多孔隈体使用号析出矩a。
As shown in these results, Comparative Example A has a large confining effect due to the diffused air, so the voltage is also low, and the stirring effect is poor. The analysis is rather slow (compared to this), but the voltage is low and it is disastrous in the non-invention, and even when used in the comparative example, three times as much copper is deposited as in the comparative example, and even more disastrous is the punching metal Q) perforated machine. When the cathode τ is used, the result is 5 times better than the one used for this porous body.

粒状とl!ll惟恨表面より容易に剥陥し、染梢郁へ沈
呻した。
Granular and l! The surface of his grudge was easily broken, and he groaned at Iku Somezou.

〔発明(1)効朱〕 以上赴へtζ如く、不発明で0.電析憎り一部τ賜水慴
−姉τ゛嵐惨荏←自己設悔としたことに工り撹拌のため
り′RL樵群下部からり直接散気方式τ赴けゐこと炉出
米、IL′鮭億朴τ越流櫃に垂直かつ8直−に配設した
りで述軟的にエアリ2トで揚水さrした篭ゼr欲rr、
均笠に、幾度となく。
[Invention (1) Efficacy] As above, it is non-inventive and 0. Part of her dislike for electrodeposition was that she used the direct aeration method from the bottom of the woodcutter group, and the furnace was launched. , IL'Salmon water was placed vertically and in eight straight lines in the overflow tank, and the water was pumped up with two air tanks.
At Junkasa, many times.

電惨也間τ流−ト、餉環すゐりで竜憔叡と金糊イオン(
1)接触も十分とれゐりで憔めて入さな篭力幼半か侍ら
fLΦO1た発生する個々リカスり布釈、放散、比込も
エアーリフトで用いらnゐ空気、不活性ガスで或し侍ゐ
ol’7t@惚も多孔性′−極と′fをことにより、胤
極間τ流■、儂環丁ゐ亀析敵り攬件効釆が史に籏lり人
備な電力効率上昇か図れ罠。
Denzaiyama τ style, Suiri Sui, Ryuukiei and Kinnori Ion (
1) Since the contact is sufficiently strong, the individual leakage, dissipation, dissipation, and concentration that occur in the case of a child or a samurai that cannot be used in an air lift can be avoided with air or an inert gas. The samurai ol' 7t @ love is also porous '-pole and 'f, so between the seed pole τ flow ■, my ring Dingi Kame analysis enemy effect is the most human power in history. A trap to increase efficiency.

4、区間り聞早々説明 ム 才1凶、第)図Qコ本発明の電析債の助囲図及び平If
II8I、第3図及び第4図に応用例の防向図。
4. A quick explanation of the section.
II8I, Fig. 3 and Fig. 4 are defensive diagrams of applied examples.

第5因は不発明り比較例り朗面凶であめ0第6図a本発
明り某施例、比叔力の処理粕禾τボ丁グランである。
The fifth factor is non-invention, comparative examples, positive aspects and negative aspects.

イ′+T3qノ配吃明 1 篭伯憤 2 崗櫨 6 エアーリント用敵気官4 坊水情 5a 岨竹用1−便値硅 5b ゛−析用展傷仏群6 
嵐住奸配設惜 7 電析金属集積都8 ′透析S1を鵜
 9 領環嵐析猷水鵡LTO%泡
I'+T3q no arrangement 1 Keibo Wrath 2 Gangbang 6 Air Lint Enemy Qikan 4 Bosuijyo 5a Atake 1-Fujiki 5b ゛-Analysis Expanded Scars Buddha Group 6
7 Electrodeposition metal accumulation capital 8 'Dialysis S1 cormorant 9 Territory ring Arashi analysis 猷水韡LTO% foam

Claims (1)

【特許請求の範囲】 1、 上端部に越流堰を備えた隔壁rcLり僧τ紙部τ
連通させて分画し、−憎τ電析&循環用のエアーリント
用散気青τ設けた揚水憎となし、他憎τ複数(/、l電
析用電極板が越流堰に垂直〃)つ鉛直に配設さn、脆水
ざγした電析敵がtm極板間τ訛下す/)篭愉群配設憎
となし、僧低都に析出金属の集積s?rtdけたC2と
τ肴偵と丁ゐ金輌イオン含有廃敵の電?1悄。 2、 1JL析用電愉82が継象#壮小醜諭カ多孔板で
あることτ轡倣とす/b金輌イオン含有廃叡り電析憎。
[Scope of Claims] 1. Partition wall rcL having an overflow weir at the upper end part τ paper part τ
The electrode plates for electrodeposition are perpendicular to the overflow weir. ) are arranged vertically, and the brittle water is deposited between the electrode plates. RTD Kept C2 and τ Appetizer and Dingi Metal Ion-containing Abandoned Enemy Den? 1 trepidation. 2, 1 JL electrodeposition electrode 82 is a successor to the perforated plate containing metal ions.
JP9036984A 1984-05-07 1984-05-07 Electrodeposition cell of waste liquid containing metallic ion Granted JPS60234989A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9036984A JPS60234989A (en) 1984-05-07 1984-05-07 Electrodeposition cell of waste liquid containing metallic ion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9036984A JPS60234989A (en) 1984-05-07 1984-05-07 Electrodeposition cell of waste liquid containing metallic ion

Publications (2)

Publication Number Publication Date
JPS60234989A true JPS60234989A (en) 1985-11-21
JPS6312153B2 JPS6312153B2 (en) 1988-03-17

Family

ID=13996636

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9036984A Granted JPS60234989A (en) 1984-05-07 1984-05-07 Electrodeposition cell of waste liquid containing metallic ion

Country Status (1)

Country Link
JP (1) JPS60234989A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008200636A (en) * 2007-02-21 2008-09-04 Mhi Environment Engineering Co Ltd Water treatment method and apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008200636A (en) * 2007-02-21 2008-09-04 Mhi Environment Engineering Co Ltd Water treatment method and apparatus

Also Published As

Publication number Publication date
JPS6312153B2 (en) 1988-03-17

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