JP2001149941A - Treating device of metal-containing waste water - Google Patents

Treating device of metal-containing waste water

Info

Publication number
JP2001149941A
JP2001149941A JP33596799A JP33596799A JP2001149941A JP 2001149941 A JP2001149941 A JP 2001149941A JP 33596799 A JP33596799 A JP 33596799A JP 33596799 A JP33596799 A JP 33596799A JP 2001149941 A JP2001149941 A JP 2001149941A
Authority
JP
Japan
Prior art keywords
waste liquid
metal
electrode plate
negative electrode
positive electrode
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
JP33596799A
Other languages
Japanese (ja)
Inventor
Munehiro Kondo
宗浩 近藤
Toshinobu Makuta
俊信 幕田
Masashi Yamamoto
正史 山本
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.)
Hitachi Chemical Techno Plant Ltd
Resonac Corp
Original Assignee
Hitachi Chemical Co Ltd
Hitachi Chemical Techno Plant 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, Hitachi Chemical Techno Plant Ltd filed Critical Hitachi Chemical Co Ltd
Priority to JP33596799A priority Critical patent/JP2001149941A/en
Publication of JP2001149941A publication Critical patent/JP2001149941A/en
Pending legal-status Critical Current

Links

Classifications

    • Y02W30/54

Landscapes

  • Water Treatment By Electricity Or Magnetism (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a treating device of metal-containing waste water for treating waste water containing metal with high efficiency and recovering the metal in the waste liquid at a high content ratio. SOLUTION: The treating device of metal-containing waste liquid is provided with a waste liquid treating tank for housing the waste liquid containing metal, a single or plural positive electrode plates installed to immerse it or them in the waste liquid, a single or plural negative plates being rotatable by being confronted with the positive electrode plates and connected with a revolving shaft, and a scraper fox peeling off deposition deposited on the negative electrode plates and obtaining a recovery product.

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、めっき廃液等の金
属を含む廃液の処理装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for treating a waste liquid containing a metal such as a plating waste liquid.

【0002】[0002]

【従来の技術】めっき廃液等の金属を含む廃液から、金
属を除去する処理法として、中和沈殿法がある。これ
は、廃液のpHを酸またはアルカリの添加によって中性
域に調整し、廃液中に溶解する金属を難溶性の水酸化物
として沈殿分離する方法である。また、金属とキレート
化合物を生成する薬液を添加するキレート添加処理法も
ある。この他に、金属を含む廃液に正極板及び負極板を
浸漬して通電する電析処理法がある。これは、廃液中に
イオンとして溶解している金属を、負極板上で電荷の無
い金属に還元することによって負極板上に析出させ、負
極板から剥離して回収する方法である。
2. Description of the Related Art As a treatment method for removing metals from a waste liquid containing metals such as plating waste liquid, there is a neutralization precipitation method. This is a method in which the pH of the waste liquid is adjusted to a neutral range by adding an acid or an alkali, and the metal dissolved in the waste liquid is precipitated and separated as a hardly soluble hydroxide. There is also a chelate addition treatment method in which a chemical solution that produces a metal and a chelate compound is added. In addition, there is an electrodeposition treatment method in which a positive electrode plate and a negative electrode plate are immersed in a waste liquid containing a metal and energized. This is a method in which a metal dissolved as an ion in a waste liquid is reduced to a metal having no charge on the negative electrode plate to precipitate on the negative electrode plate, and is separated and recovered from the negative electrode plate.

【0003】[0003]

【発明が解決しようとする課題】従来の技術のうち、中
和沈殿法では、装置に要する機器が少なく、装置コスト
が安価であるが、廃液のpHが強酸または強アルカリの
場合、多量の薬液で中和する必要があり運転コストが高
価となる可能性があり、また、この処理によって発生し
た金属水酸化物スラッジを、有価物として回収する場
合、金属水酸化物スラッジは含水率が高いために、脱水
または乾燥を行う装置が必要であり、さらに、これによ
って得られた金属水酸化物スラッジが、金属が単体では
なく水酸化物として存在し、廃液の種類によっては金属
水酸化物以外の物質が混在するために金属の含有率が低
く、有価物として販売する際の単価が非常に安価とな
り、結局、運搬の費用の方が高くなってしまい、引取り
費用が発生することが多いという課題がある。
Among the conventional techniques, in the neutralization precipitation method, the equipment required for the apparatus is small and the cost of the apparatus is low. However, when the pH of the waste liquid is a strong acid or a strong alkali, a large amount of chemical solution is required. It is necessary to neutralize with, there is a possibility that the operating cost may be expensive, and also, when the metal hydroxide sludge generated by this treatment is recovered as a valuable resource, the metal hydroxide sludge has a high water content. In addition, a device that performs dehydration or drying is required, and furthermore, the metal hydroxide sludge obtained by this means that the metal is present not as a simple substance but as a hydroxide, and depending on the type of waste liquid, other than a metal hydroxide. Due to the mixture of substances, the content of metals is low, the unit price when selling as valuable resources becomes very low, and eventually the transportation cost becomes higher, and collection costs may occur. There is a problem that had.

【0004】また、キレート添加処理法では、キレート
剤と呼ばれるこれらの薬液が高価であるため、運転コス
トが高価であり、また、生成する金属キレート化合物ス
ラッジを有価物として回収するときに、中和沈殿法と同
ように、引取りの費用が発生するという課題がある。
[0004] In addition, in the chelate addition treatment method, since these chemicals called chelating agents are expensive, the operating cost is high, and when the produced metal chelate compound sludge is recovered as valuables, it is neutralized. As in the case of the sedimentation method, there is a problem that a collection cost is required.

【0005】また、電析処理法では、多量の薬液を必要
とせず、回収物の含水率が低いため有価回収を行う際に
脱水及び乾燥を行うための装置が不要で、回収物中の金
属含有率が高く、有価物として販売する際の単価が高価
となるので、前述の2つの方法と比較して優れている
が、負極板上の析出物の剥離作業が人手と時間を要する
作業であり、そのために実施された例は極めて少ないの
が現状であった。
[0005] In addition, the electrodeposition treatment method does not require a large amount of a chemical solution and has a low water content in the recovered material, so that a device for performing dehydration and drying when recovering valuable resources is unnecessary, and the metal in the recovered material is not required. Since the content rate is high and the unit price when selling it as a valuable resource is expensive, it is superior to the above two methods, but the work of stripping the precipitate on the negative electrode plate requires labor and time. At present, very few examples have been implemented for that purpose.

【0006】本発明は、電析処理法の改良に関するもの
であり、効率に優れた、金属を含む廃液を処理すると共
に、廃液中の金属を高い含有率で回収できる金属含有廃
液の処理装置を提供することを目的とする。
The present invention relates to an improvement in an electrodeposition treatment method, and more particularly to an apparatus for treating a metal-containing waste liquid which is excellent in efficiency and can treat a metal-containing waste liquid and can recover a high content of metal in the waste liquid. The purpose is to provide.

【0007】[0007]

【課題を解決するための手段】本発明は、金属を含む廃
液を収容する廃液処理槽と、この廃液に浸漬するように
設置された単一または複数の正極板と、この正極板と対
向し回転軸で連結されることにより、回転可能である単
一または複数の負極板と、この負極板上に析出した析出
物を剥離して回収物を得るスクレーパを備えた金属含有
廃液の処理装置である。
SUMMARY OF THE INVENTION The present invention is directed to a waste liquid treatment tank containing a waste liquid containing a metal, a single or a plurality of positive plates installed so as to be immersed in the waste liquid, and a plate facing the positive plate. By being connected by a rotating shaft, a rotatable single or multiple negative plates, and a metal-containing waste liquid treatment device equipped with a scraper that separates deposits deposited on the negative plates to obtain a recovered product is there.

【0008】[0008]

【発明の実施の形態】以下に本発明の実施の形態を図1
に基づいて説明する。廃液8は、めっき廃液のように金
属を含む廃液である。金属の濃度の高低に関わらず適用
可能であるが、廃液中に通電を行うために、廃液中に適
度の電解質が溶解していることが望ましい。廃液処理槽
5は、廃液8を収容し、正極板1と負極板2の一部を浸
漬することが可能な容積を有するものである。また、廃
液処理槽5内の金属濃度分布を一定とするために、必要
に応じてばっ気等の手段(図示せず)により槽内を攪拌
することが好ましい。正極板1は、廃液処理槽5内で負
極板2と対向するように設け、極板枚数が複雑となる場
合は、負極板2と交互に設けることができる。正極板1
の材質は、処理する廃液の種類によっても異なるが、耐
食性の金属板やカーボン板が適用できる。カーボン板
は、軽量且つ安価であるが、廃液8によっては、カーボ
ンが廃液8中に溶解して、正極板1の損耗が激しい場合
がある。このような場合は、チタン等の不溶性の金属板
を使用することが望ましい。負極板2は、廃液処理槽5
内で正極板1と対向するように設け、回転軸4で支持し
て回転可能とする。極板枚数が複雑となる場合には、同
一の回転軸4で支持し、正極板1と交互に設ける。負極
板2の材質は、耐食性の金属板が適用可能であり、特に
ステンレスが望ましい。回転軸4は、負極板2に電流を
供給するための導線の役割も有し、正極板1の近傍にお
ける短絡を防ぐために、その外周を絶縁体で覆う。負極
板2の回転時に析出物6がスクレーパ3によって剥離す
る。スクレーパ3は、鋼板が適用可能である。また、ス
クレーパ3は、斜度を設けて設置し、負極板2から剥離
した回収物7を装置外へ移送する役割も有する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to FIG.
It will be described based on. The waste liquid 8 is a waste liquid containing a metal such as a plating waste liquid. Although it can be applied regardless of the concentration of the metal, it is desirable that an appropriate amount of electrolyte is dissolved in the waste liquid in order to conduct electricity in the waste liquid. The waste liquid treatment tank 5 has a capacity that accommodates the waste liquid 8 and can immerse a part of the positive electrode plate 1 and a part of the negative electrode plate 2. Further, in order to keep the metal concentration distribution in the waste liquid treatment tank 5 constant, it is preferable to stir the inside of the tank by means such as aeration (not shown) as necessary. The positive electrode plate 1 is provided so as to face the negative electrode plate 2 in the waste liquid treatment tank 5. If the number of the electrode plates becomes complicated, the positive electrode plate 1 can be provided alternately with the negative electrode plate 2. Positive electrode plate 1
The material varies depending on the type of waste liquid to be treated, but a corrosion-resistant metal plate or carbon plate can be used. Although the carbon plate is lightweight and inexpensive, depending on the waste liquid 8, carbon may be dissolved in the waste liquid 8 and the positive electrode plate 1 may be severely worn. In such a case, it is desirable to use an insoluble metal plate such as titanium. The negative electrode plate 2 includes a waste liquid treatment tank 5
It is provided so as to face the positive electrode plate 1 and is rotatable while being supported by the rotating shaft 4. When the number of electrode plates is complicated, they are supported by the same rotating shaft 4 and provided alternately with the positive electrode plate 1. As the material of the negative electrode plate 2, a corrosion-resistant metal plate can be used, and stainless steel is particularly desirable. The rotating shaft 4 also has a role of a conducting wire for supplying a current to the negative electrode plate 2, and its outer periphery is covered with an insulator to prevent a short circuit near the positive electrode plate 1. The precipitate 6 is peeled off by the scraper 3 when the negative electrode plate 2 rotates. As the scraper 3, a steel plate can be applied. Further, the scraper 3 is installed with an inclination, and also has a role of transferring the collected material 7 separated from the negative electrode plate 2 to the outside of the device.

【0009】[0009]

【実施例】実際にめっき廃液を処理した事例について説
明する。表1に、処理対象廃液の内容を示す。
EXAMPLE An example in which a plating waste liquid is actually treated will be described. Table 1 shows the contents of the waste liquid to be treated.

【0010】[0010]

【表1】 [Table 1]

【0011】以下に、装置の諸元を示す。 ・廃液処理槽: 大きさ=300mmラ900mmラ500mm、有効容積
=110リットル ・正極板: 形状=直径800mmの半円板、厚さ=20mm、材質
=チタン、枚数=2枚、有効極板面積=0.75m2 ・負極板: 形状=直径800mmの円板、厚さ=30mm、材質=
ステンレス、枚数=2枚、有効極板面積=0.75m2
The specifications of the apparatus will be described below.・ Waste liquid treatment tank: Size = 300mm × 900mm × 500mm, effective volume = 110 liter ・ Positive electrode plate: Shape = semicircle with diameter of 800mm, thickness = 20mm, material = titanium, number of sheets = 2, effective electrode plate area = 0.75 m 2 · Negative electrode plate: Shape = disk with a diameter of 800 mm, thickness = 30 mm, material =
Stainless steel, number of sheets = 2, effective electrode plate area = 0.75 m 2

【0012】図1に示す廃液処理槽5の廃液8に、正極
板のほとんどを浸漬し、負極板の下半分を廃液に浸漬す
る。正極板、負極板の枚数は、それぞれ2枚であるが、
廃液中で正極板と負極板が対向する面はそれぞれ3面で
あるため、有効極板面積は正極板の面積の3倍の数値と
なる。このような装置において、正極板と負極板との間
に600Aの直流電流を通電した。処理水中のニッケル
濃度は、2時間後には450mg/l(除去率93
%)、4時間後には110mg/l(除去率98%)、
8時間後には20mg/l(除去率99.7%)まで低
下した。スクレーパによって剥離回収した回収物のニッ
ケル含有率は、回収物の乾燥重量に対する重量割合で8
2%であった。
Most of the positive electrode plate is immersed in the waste liquid 8 of the waste liquid treatment tank 5 shown in FIG. 1, and the lower half of the negative electrode plate is immersed in the waste liquid. The number of the positive electrode plate and the negative electrode plate is two, respectively.
Since the surfaces of the positive electrode plate and the negative electrode plate facing each other in the waste liquid are respectively three, the area of the effective electrode plate is three times the area of the positive electrode plate. In such an apparatus, a DC current of 600 A was applied between the positive electrode plate and the negative electrode plate. The nickel concentration in the treated water was 450 mg / l after 2 hours (93% removal rate).
%) 110 mg / l (removal rate 98%) after 4 hours,
After 8 hours, the concentration had dropped to 20 mg / l (a removal rate of 99.7%). The nickel content of the recovered material separated and recovered by the scraper was 8% by weight based on the dry weight of the recovered material.
2%.

【0013】この金属含有廃液の処理装置によれば、回
転可能である単一または複数の負極板と、この負極板上
に析出した物を剥離して回収物を得るスクレーパを備え
たことによって、負極板上の析出物の剥離作業を自動化
することができ、多量の薬液を使用せずに金属成分を含
む廃液を処理することが可能である。また、処理に伴っ
て回収される回収物は、含水率が小さく且つ金属成分の
含有率が高いため、脱水または乾燥等の後処理を行わず
に有価物として回収できる。
According to the apparatus for treating a metal-containing waste liquid, a single or a plurality of rotatable negative electrode plates and a scraper for removing a substance deposited on the negative electrode plate to obtain a recovered material are provided. The operation of separating the precipitate on the negative electrode plate can be automated, and a waste liquid containing a metal component can be treated without using a large amount of a chemical solution. In addition, the collected material collected during the treatment has a low water content and a high metal component content, and thus can be collected as a valuable material without performing post-treatment such as dehydration or drying.

【0014】[0014]

【発明の効果】以上に説明したとおり、本発明によっ
て、効率に優れた、金属を含む廃液を処理すると共に、
廃液中の金属を高い含有率で回収できる金属含有廃液の
処理装置を提供することができる。
As described above, according to the present invention, it is possible to treat highly efficient waste liquid containing metal,
It is possible to provide an apparatus for treating a metal-containing waste liquid capable of recovering a high content of metals in the waste liquid.

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

【図1】(a)は、本発明の一実施例の要部を示す斜視
図であり、(b)は、装置全体の概要を示す正面図であ
る。
FIG. 1A is a perspective view showing a main part of an embodiment of the present invention, and FIG. 1B is a front view showing an outline of the entire apparatus.

【符号の説明】[Explanation of symbols]

1.正極板 2.負極板 3.スクレーパ 4.回転軸 5.廃液処理槽 6.析出物 7.回収物 8.廃液 1. 1. positive electrode plate Negative electrode plate 3. Scraper 4. Rotation axis 5. Waste liquid treatment tank 6. Precipitate 7. Collected items 8. Waste liquid

───────────────────────────────────────────────────── フロントページの続き (72)発明者 幕田 俊信 茨城県下館市大字下江連1250番地 日立化 成テクノプラント株式会社内 (72)発明者 山本 正史 茨城県下館市大字下江連1250番地 日立化 成テクノプラント株式会社内 Fターム(参考) 4D061 DA08 DB18 DC20 EA05 EB20 EB28 EB30 EB33 ED20 4K001 AA19 BA21 DB21  ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Toshinobu Makita 1250 Shimoedori, Shimodate-shi, Ibaraki Prefecture Within Hitachi Chemical Technoplant Co., Ltd. (72) Inventor Masashi Yamamoto 1250 Shimoedori, Shimodate-shi, Ibaraki Hitachi Techno Plant Co., Ltd. F term (reference) 4D061 DA08 DB18 DC20 EA05 EB20 EB28 EB30 EB33 ED20 4K001 AA19 BA21 DB21

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】金属を含む廃液を収容する廃液処理槽と、
この廃液に浸漬するように設置された単一または複数の
正極板と、この正極板と対向し回転軸で連結されること
により回転可能である単一または複数の負極板と、この
負極板上に析出した析出物を剥離して回収物を得るスク
レーパを備えたことを特徴とする金属含有廃液の処理装
置。
1. A waste liquid treatment tank containing a waste liquid containing metal,
A single or a plurality of positive plates placed so as to be immersed in the waste liquid, a single or a plurality of negative plates which are rotatable by being connected to a rotating shaft facing the positive plate, and on the negative plate; An apparatus for treating a metal-containing waste liquid, comprising: a scraper for separating a precipitate deposited on a surface to obtain a recovered product.
JP33596799A 1999-11-26 1999-11-26 Treating device of metal-containing waste water Pending JP2001149941A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33596799A JP2001149941A (en) 1999-11-26 1999-11-26 Treating device of metal-containing waste water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33596799A JP2001149941A (en) 1999-11-26 1999-11-26 Treating device of metal-containing waste water

Publications (1)

Publication Number Publication Date
JP2001149941A true JP2001149941A (en) 2001-06-05

Family

ID=18294333

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33596799A Pending JP2001149941A (en) 1999-11-26 1999-11-26 Treating device of metal-containing waste water

Country Status (1)

Country Link
JP (1) JP2001149941A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002119985A (en) * 2000-10-12 2002-04-23 Fuji Clean Kogyo Kk Apparatus and method for treating wastewater
JP2007063656A (en) * 2005-09-02 2007-03-15 Kokubu Nagayoshi Electrolytic treatment apparatus
JP2013119050A (en) * 2011-12-06 2013-06-17 Disco Corp Waste liquid treatment apparatus
CN105836849A (en) * 2015-01-16 2016-08-10 宜兴市凌泰环保设备有限公司 High efficiency electrocatalytic electrode coaxial rotation reaction device
CN110894088A (en) * 2019-12-31 2020-03-20 王兆兵 Self-cleaning electrolytic device

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002119985A (en) * 2000-10-12 2002-04-23 Fuji Clean Kogyo Kk Apparatus and method for treating wastewater
JP2007063656A (en) * 2005-09-02 2007-03-15 Kokubu Nagayoshi Electrolytic treatment apparatus
JP4649681B2 (en) * 2005-09-02 2011-03-16 圀武 永良 Electrolytic treatment equipment
JP2013119050A (en) * 2011-12-06 2013-06-17 Disco Corp Waste liquid treatment apparatus
CN105836849A (en) * 2015-01-16 2016-08-10 宜兴市凌泰环保设备有限公司 High efficiency electrocatalytic electrode coaxial rotation reaction device
CN110894088A (en) * 2019-12-31 2020-03-20 王兆兵 Self-cleaning electrolytic device

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