JP2018044189A - Electrolysis defatting method and electrolysis defatting device - Google Patents

Electrolysis defatting method and electrolysis defatting device Download PDF

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JP2018044189A
JP2018044189A JP2016177770A JP2016177770A JP2018044189A JP 2018044189 A JP2018044189 A JP 2018044189A JP 2016177770 A JP2016177770 A JP 2016177770A JP 2016177770 A JP2016177770 A JP 2016177770A JP 2018044189 A JP2018044189 A JP 2018044189A
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cleaned
electrolyzed water
alkaline electrolyzed
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JP6479729B2 (en
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小川 健二
Kenji Ogawa
健二 小川
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FUDAUCHI KOGYO CO Ltd
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Priority to MX2018014618A priority patent/MX370832B/en
Priority to PCT/JP2017/030741 priority patent/WO2018047654A1/en
Priority to CN201780036041.8A priority patent/CN109415838B/en
Priority to TW106130795A priority patent/TWI647346B/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B3/00Cleaning by methods involving the use or presence of liquid or steam
    • B08B3/04Cleaning involving contact with liquid
    • B08B3/08Cleaning involving contact with liquid the liquid having chemical or dissolving effect
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B3/00Cleaning by methods involving the use or presence of liquid or steam
    • B08B3/04Cleaning involving contact with liquid
    • B08B3/10Cleaning involving contact with liquid with additional treatment of the liquid or of the object being cleaned, e.g. by heat, by electricity or by vibration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B3/00Cleaning by methods involving the use or presence of liquid or steam
    • B08B3/04Cleaning involving contact with liquid
    • B08B3/10Cleaning involving contact with liquid with additional treatment of the liquid or of the object being cleaned, e.g. by heat, by electricity or by vibration
    • B08B3/12Cleaning involving contact with liquid with additional treatment of the liquid or of the object being cleaned, e.g. by heat, by electricity or by vibration by sonic or ultrasonic vibrations
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/34Treatment of water, waste water, or sewage with mechanical oscillations
    • C02F1/36Treatment of water, waste water, or sewage with mechanical oscillations ultrasonic vibrations
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G1/00Cleaning or pickling metallic material with solutions or molten salts
    • C23G1/14Cleaning or pickling metallic material with solutions or molten salts with alkaline solutions
    • C23G1/19Iron or steel
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23GCLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
    • C23G3/00Apparatus for cleaning or pickling metallic material
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25FPROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
    • C25F1/00Electrolytic cleaning, degreasing, pickling or descaling
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25FPROCESSES FOR THE ELECTROLYTIC REMOVAL OF MATERIALS FROM OBJECTS; APPARATUS THEREFOR
    • C25F7/00Constructional parts, or assemblies thereof, of cells for electrolytic removal of material from objects; Servicing or operating

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Materials Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Electrochemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
  • Cleaning By Liquid Or Steam (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)
  • Physical Water Treatments (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an electrolysis defatting method capable of more surely removing contaminants such as an oil component from a surface of an objection to be cleaned without generating reattachment of removed contaminants to the object to be cleaned and an electrolysis defatting device using the same.SOLUTION: There are adopted an electrolysis defatting method for removing contaminants such as an oil component adhered to an object to be cleaned by using an alkaline electrolytic water, including arranging the object to be cleaned and an anode electrode in an alkaline electrolytic water and energizing them, cathode polarizing the object to be cleaned to form hydrogen bubbles with diameter of 20 nm to 10 μm on a surface of the object to be cleaned, and breaking the hydrogen bubbles in vicinity of the surface of the object to be cleaned to conduct removal of the contaminants adhered to the surface of the object to be cleaned by an impulse wave do to the breakage, the anode electrode has an electrode catalyst layer containing iridium oxide of 20 g/mon a surface thereof, and an electrolysis defatting device for conducting the method.SELECTED DRAWING: Figure 1

Description

本件出願にかかる発明は、被洗浄対象物の表面に付着した汚染物除去を行うための電解脱脂方法、及び、その電解脱脂方法を実施するための電解脱脂装置に関する。   The invention according to the present application relates to an electrolytic degreasing method for removing contaminants attached to the surface of an object to be cleaned, and an electrolytic degreasing apparatus for carrying out the electrolytic degreasing method.

一般に、工業部品の表面にめっき処理や塗装処理を施す場合には、被処理面に存在する汚染物質の除去を行う必要があり、めっき処理や塗装処理を施す前処理として工業部品の表面に存在する汚染物質の除去処理を行う。汚染物質の多くは、製造過程において使用される水溶性油や非水系油等の油分である。これら汚染物質が工業部品の表面に残存していると、めっきや塗装の皮膜自体の形成が不可能となったり、仮にめっきや塗装の皮膜が形成出来た場合であっても、その膜厚に大きなバラツキが生じてしまう。   Generally, when plating or painting treatment is performed on the surface of an industrial part, it is necessary to remove contaminants present on the surface to be treated. To remove the pollutants. Most of the pollutants are oils such as water-soluble oils and non-aqueous oils used in the production process. If these contaminants remain on the surface of industrial parts, it is impossible to form a plating or coating film, or even if a plating or coating film can be formed, Large variations will occur.

そこで、従来より、工業部品の表面にめっき処理や塗装処理を施す前処理として、脱脂処理が採用されている。脱脂の方法としては、アルカリ脱脂や、電解脱脂等がある。アルカリ脱脂は、水酸化物や、リン酸塩、ケイ酸塩、炭酸塩等の各種アルカリ化合物と、界面活性剤を主に含むアルカリ脱脂液中に、被処理対象物を浸漬して行う。電解脱脂は、アルカリ脱脂と同様に、アルカリ脱脂液を用い、被処理対象物を電解にし、表面に発生するガスにより物理的に汚れを除去する。被処理対象物を陰極とした場合には、表面に発生する水素ガスによって、表面の汚れを物理的に除去し、被処理対象物を陽極とした場合には、表面に発生する酸素ガスによって、表面の汚れを酸化・分解して汚れを除去する。   Therefore, degreasing treatment has been conventionally employed as a pretreatment for performing plating treatment or coating treatment on the surface of industrial parts. Degreasing methods include alkali degreasing and electrolytic degreasing. Alkaline degreasing is performed by immersing an object to be treated in an alkaline degreasing solution mainly containing a hydroxide, various alkali compounds such as phosphates, silicates, and carbonates, and a surfactant. Similarly to alkaline degreasing, electrolytic degreasing uses an alkaline degreasing solution to electrolyze the object to be treated, and physically removes dirt by gas generated on the surface. When the object to be treated is a cathode, the surface is physically removed by hydrogen gas generated on the surface, and when the object to be treated is an anode, oxygen gas generated on the surface is used. The dirt on the surface is oxidized and decomposed to remove the dirt.

例えば、電解脱脂方法を採用した従来技術として特許文献1がある。特許文献1には、「油、錆、汚れ等の異物を表面に有する導電性部材を陰極とし、金属電極を陽極とし、前記陽極及び前記陰極を電解液に浸漬する工程と、前記電解液中の陽極と前記陰極との間に電圧を印加して両電極間に電流を流すことにより、前記導電性部材表面に連続的に気泡を生じさせる工程と、当該気泡による機械的撹拌により、前記導電性部材表面から前記異物を除去させる工程とを含んでいることを特徴とする導電性部材の電解脱脂方法」が開示されている。   For example, there is Patent Document 1 as a prior art employing an electrolytic degreasing method. In Patent Document 1, “a conductive member having foreign matters such as oil, rust, and dirt on its surface is used as a cathode, a metal electrode is used as an anode, and the anode and the cathode are immersed in an electrolytic solution; By applying a voltage between the anode and the cathode and causing a current to flow between the two electrodes to continuously generate bubbles on the surface of the conductive member, and mechanical agitation with the bubbles, And a step of removing the foreign matter from the surface of the conductive member. An electrolytic degreasing method for a conductive member is disclosed.

特開平10−245700号公報Japanese Patent Laid-Open No. 10-245700

しかしながら、上述のような特許文献1では、アルカリ脱脂液である電解液を電解することにより陰極とした導電性部材の表面から発生した水素ガスによる機械的撹拌と陰極還元により、導電性部材表面の異物を除去するものであるため、複雑な微細凹凸を表面に備えた導電性部材の異物を除去することができなかった。なぜならば、アルカリ化合物と界面活性剤を含む電解液を電解した場合に導電性部材の表面から発生する水素ガスは、比較的大きく、導電性部材の表面に当該気泡よりも小さな凹部が存在すると、当該凹部内に当該気泡が侵入することが出来ないからである。   However, in Patent Document 1 as described above, the surface of the conductive member is subjected to mechanical stirring and cathode reduction with hydrogen gas generated from the surface of the conductive member serving as a cathode by electrolyzing an electrolytic solution that is an alkaline degreasing solution. Since the foreign matter is to be removed, the foreign matter of the conductive member having complicated fine irregularities on the surface could not be removed. This is because the hydrogen gas generated from the surface of the conductive member when the electrolytic solution containing the alkali compound and the surfactant is electrolyzed is relatively large, and there is a recess smaller than the bubbles on the surface of the conductive member. This is because the bubbles cannot enter the recess.

また、特許文献1では、電解脱脂によって、導電性部材表面から除去された油分等の異物は、電解液中に浮遊しているため、当該電解液から導電性部材を引き上げる際に、再度その表面に分離した異物が付着し、次工程を行う槽内に異物が持ち込まれる不都合があった。さらに、当該油分等の濃度が高まった電解液は、廃水処理が煩雑となる問題があった。   Moreover, in patent document 1, since foreign substances, such as the oil component removed from the electroconductive member surface by electrolytic degreasing, are floating in electrolyte solution, when pulling up the electroconductive member from the electrolyte solution, the surface again There is a problem that the separated foreign matter adheres to the tank and the foreign matter is brought into the tank where the next process is performed. Furthermore, the electrolytic solution in which the concentration of the oil or the like is increased has a problem that wastewater treatment becomes complicated.

以上のことから、市場からは、被洗浄対象物がその表面に複雑な微細凹凸を備えている場合でも、より確実に油分等の汚染物質の除去が可能で、除去した汚染物質が被洗浄対象物に再付着する不都合を解消することができる電解脱脂方法及び電解脱脂装置の開発が望まれていた。   From the above, it is possible to remove contaminants such as oil more reliably even if the object to be cleaned has complex fine irregularities on the surface. It has been desired to develop an electrolytic degreasing method and an electrolytic degreasing apparatus that can eliminate the inconvenience of being reattached to an object.

そこで、鋭意研究の結果、以下に述べる如き電解脱脂方法及び電解脱脂装置を採用することに想到した。   Therefore, as a result of intensive studies, the inventors have come to the idea of adopting an electrolytic degreasing method and an electrolytic degreasing apparatus as described below.

電解脱脂方法: 本件出願にかかる電解脱脂方法は、アルカリ性電解水を用いて被洗浄対象物の表面に付着した油分等の汚染物を除去する脱脂方法であって、アルカリ性電解水中に被洗浄対象物とアノード電極とを配置し通電することで、被洗浄対象物をカソード分極して、被洗浄対象物の表面に直径20nm〜10μmの水素バブルを形成し、被洗浄対象物の表面近傍で水素バブルを破壊させ、当該破壊に伴う衝撃波(キャビテーション現象)により被洗浄対象物の表面に付着した汚染物除去を行うものであり、当該アノード電極は、その表面に10g/m〜20g/m量の酸化イリジウムを含有する電極触媒層を有することを特徴とするものである。 Electrolytic degreasing method: The electrolytic degreasing method according to the present application is a degreasing method for removing contaminants such as oil adhering to the surface of an object to be cleaned using alkaline electrolyzed water, and the object to be cleaned in alkaline electrolyzed water. The anode to be cleaned is cathode-polarized to form a hydrogen bubble having a diameter of 20 nm to 10 μm on the surface of the object to be cleaned, and a hydrogen bubble near the surface of the object to be cleaned. was destroyed, which performs contaminant removal adhering to the surface of the cleaned object by shock waves (cavitation) accompanying such destruction, the anode electrode, 10g / m 2 ~20g / m 2 amount on the surface thereof And an electrode catalyst layer containing iridium oxide.

本件出願にかかる電解脱脂方法において、前記アルカリ性電解水は、炭酸カリウム及び水酸化カリウムを含むpH11〜pH13の水溶液を用いることが好ましい。   In the electrolytic degreasing method according to the present application, the alkaline electrolyzed water is preferably an aqueous solution having a pH of 11 to 13 containing potassium carbonate and potassium hydroxide.

本件出願にかかる電解脱脂方法において、被洗浄対象物の表面近傍での水素バブルの破壊は、当該水素バブルに対して、アルカリ性電解水中で超音波を照射することにより行うことが好ましい。   In the electrolytic degreasing method according to the present application, the destruction of the hydrogen bubble near the surface of the object to be cleaned is preferably performed by irradiating the hydrogen bubble with ultrasonic waves in alkaline electrolytic water.

本件出願にかかる電解脱脂方法は、通電中の前記アノード電極で発生したスーパーオキシドアニオンと、前記被洗浄対象物の表面から除去した油分とを、前記アルカリ性電解水中で反応させ、当該油分を炭素と二酸化炭素とに分解することが好ましい。   In the electrolytic degreasing method according to the present application, the superoxide anion generated at the anode electrode being energized and the oil removed from the surface of the object to be cleaned are reacted in the alkaline electrolyzed water, and the oil is converted to carbon. It is preferable to decompose into carbon dioxide.

電解脱脂装置: 本件出願にかかる電解脱脂装置は、上述の電解脱脂方法を用いて被洗浄対象物の表面を清浄化するための電解脱脂装置であって、アルカリ性電解水を貯液する脱脂槽と、当該脱脂槽内に配置するアノード電極と、当該アルカリ性電解水中に前記被洗浄対象物を浸漬した状態で配置し、当該被洗浄対象物をカソード分極して当該被洗浄対象物の表面に直径20nm〜10μmの水素バブルを形成するための通電手段と、当該被洗浄対象物の表面近傍の水素バブルを破壊する水素バブル破壊手段と、当該アルカリ性電解水の循環濾過手段とを備え、当該循環濾過手段は、当該脱脂槽からオーバーフローした当該アルカリ性電解水を濾過手段により濾過した後に当該脱脂槽の下部へ返送するものであることを特徴とする。 Electrolytic degreasing apparatus: The electrolytic degreasing apparatus according to the present application is an electrolytic degreasing apparatus for cleaning the surface of an object to be cleaned using the above-described electrolytic degreasing method, and a degreasing tank for storing alkaline electrolyzed water; The anode electrode disposed in the degreasing tank and the object to be cleaned are immersed in the alkaline electrolyzed water, and the object to be cleaned is cathode-polarized to have a diameter of 20 nm on the surface of the object to be cleaned. A circulating filtration means comprising: an energization means for forming a hydrogen bubble of 10 μm; a hydrogen bubble destruction means for destroying a hydrogen bubble near the surface of the object to be cleaned; and a circulating filtration means for the alkaline electrolyzed water. Is characterized in that the alkaline electrolyzed water overflowed from the degreasing tank is filtered by a filtering means and then returned to the lower part of the degreasing tank.

本件出願にかかる電解脱脂装置において、前記アノード電極には、酸化イリジウム電極を用いることが好ましい。   In the electrolytic degreasing apparatus according to the present application, it is preferable to use an iridium oxide electrode as the anode electrode.

本件出願にかかる電解脱脂装置において、前記脱脂槽は、少なくとも内面を超音波を反射可能な材質で形成し、前記アノード電極は、超音波を透過可能とする連通部を備えたことが好ましい。   In the electrolytic degreasing apparatus according to the present application, it is preferable that at least an inner surface of the degreasing tank is made of a material that can reflect ultrasonic waves, and the anode electrode includes a communication portion that can transmit ultrasonic waves.

また、本件出願にかかる電解脱脂装置において、前記水素バブル破壊手段は、被洗浄対象物の表面で発生する水素バブルに対して、アルカリ性電解水中で超音波を照射する超音波照射手段であることが好ましい。   Further, in the electrolytic degreasing apparatus according to the present application, the hydrogen bubble destruction means is an ultrasonic irradiation means for irradiating ultrasonic waves in alkaline electrolytic water against hydrogen bubbles generated on the surface of the object to be cleaned. preferable.

本件出願にかかる電解脱脂方法及び電解脱脂装置を用いることで、複雑で微細な凹凸の表面形状を備える被洗浄対象物であっても、その表面に付着した汚染物質を効果的に除去することが可能となる。しかも、当該被洗浄対象物の表面から除去した油分を、アルカリ性電解水中で炭素と二酸化炭素とに分解することができるため、除去した油分の被洗浄対象物表面への再付着が起こらなくなる。従って、本件出願にかかる電解脱脂方法及び電解脱脂装置によれば、従来の脱脂処理方法及び脱脂処理装置に比べて、格段に優れた清浄化効果を得ることができる。   By using the electrolytic degreasing method and the electrolytic degreasing apparatus according to the present application, it is possible to effectively remove the contaminants attached to the surface of the object to be cleaned even if the object has a complicated and fine uneven surface shape. It becomes possible. Moreover, since the oil removed from the surface of the object to be cleaned can be decomposed into carbon and carbon dioxide in alkaline electrolyzed water, the removed oil does not reattach to the surface of the object to be cleaned. Therefore, according to the electrolytic degreasing method and the electrolytic degreasing apparatus according to the present application, it is possible to obtain a cleaning effect that is significantly superior to the conventional degreasing treatment method and the degreasing treatment apparatus.

電解脱脂装置の一実施形態における概略説明図である。It is a schematic explanatory drawing in one Embodiment of an electrolytic degreasing apparatus. 電解脱脂装置の別の一実施形態における概略説明図である。It is a schematic explanatory drawing in another one Embodiment of an electrolytic degreasing apparatus.

以下、本件発明の実施の形態に関して、「電解脱脂方法の形態」、「電解脱脂装置の形態」の順に説明する。   Hereinafter, the embodiment of the present invention will be described in the order of “form of electrolytic degreasing method” and “form of electrolytic degreasing apparatus”.

<本件出願にかかる電解脱脂方法について>
本件出願にかかる電解脱脂方法は、アルカリ性電解水を用いて被洗浄対象物の表面に付着した油分等の汚染物を除去するものである。また、本件発明においては、アルカリ性電解水中に被洗浄対象物とアノード電極とを配置し通電することで、被洗浄対象物をカソード分極して、被洗浄対象物の表面に直径20nm〜10μmの水素バブルを形成し、被洗浄対象物の表面近傍で水素バブルを破壊させ、当該破壊に伴う衝撃波により被洗浄対象物の表面に付着した汚染物除去を行うものである。そして、本件出願にかかる電解脱脂方法は、当該アノード電極の表面に10g/m〜20g/mの量の酸化イリジウムを含有する電極触媒層を有することを特徴とする。以下、本件出願にかかる電解脱脂方法について具体的に説明する。
<About the electrolytic degreasing method according to the present application>
The electrolytic degreasing method according to the present application is to remove contaminants such as oil adhering to the surface of an object to be cleaned using alkaline electrolyzed water. Further, in the present invention, the object to be cleaned and the anode electrode are placed in the alkaline electrolyzed water and energized, so that the object to be cleaned is cathodically polarized and hydrogen having a diameter of 20 nm to 10 μm is formed on the surface of the object to be cleaned. A bubble is formed, hydrogen bubbles are destroyed in the vicinity of the surface of the object to be cleaned, and contaminants attached to the surface of the object to be cleaned are removed by a shock wave accompanying the destruction. Then, electrolytic degreasing method according to the present application is characterized by having an electrode catalyst layer containing iridium oxide in an amount surface of 10g / m 2 ~20g / m 2 of the anode electrode. Hereinafter, the electrolytic degreasing method according to the present application will be specifically described.

アルカリ性電解水: 本件発明において用いる「アルカリ性電解水」は、一般に、電解質を添加した水を、有膜式電解層内において所定の直流電流で電解処理して得られるアルカリ性を呈する水溶液である。被洗浄対象物とアノード電極とをアルカリ性電解水中に配置し通電した際に、被洗浄対象物の表面に水素のマイクロナノバブルを形成することを考慮すると、当該アルカリ性電解水は、炭酸カリウム及び水酸化カリウムを添加したものであることが好ましい。 Alkaline electrolyzed water: “Alkaline electrolyzed water” used in the present invention is generally an aqueous solution exhibiting alkalinity obtained by subjecting water to which an electrolyte is added to electrolysis with a predetermined direct current in a membrane-type electrolytic layer. Considering the formation of hydrogen micro-nano bubbles on the surface of the object to be cleaned when the object to be cleaned and the anode electrode are placed in alkaline electrolyzed water and energized, the alkaline electrolyzed water is composed of potassium carbonate and hydroxide. It is preferable that potassium is added.

更に、当該被洗浄対象物の表面から除去した油分を、アルカリ性電解水中で炭素と二酸化炭素とに分解することを考慮すると、当該アルカリ性電解水は、pH11〜pH13であることが好ましい。pH11以上のアルカリ性電解水でなければ、アルカリ脱脂としての効果が十分に発揮されず、工業的に要求される生産効率を得られない。一方、pH13を超えるアルカリ性電解水を用いても、アルカリ脱脂効果は飽和し、薬剤の無駄となるため好ましくない。   Furthermore, considering that the oil removed from the surface of the object to be cleaned is decomposed into carbon and carbon dioxide in alkaline electrolyzed water, the alkaline electrolyzed water is preferably pH 11 to pH 13. Unless the alkaline electrolyzed water has a pH of 11 or more, the effect of alkaline degreasing is not sufficiently exhibited, and industrially required production efficiency cannot be obtained. On the other hand, using alkaline electrolyzed water exceeding pH 13 is not preferable because the alkaline degreasing effect is saturated and the chemical is wasted.

なお、このアルカリ性電解水を調製する際には、「純度99.9質量%以上のアルカリ性電解水」を用いることが好ましい。「純度99.9質量%未満のアルカリ性電解水」を用いた場合、水に含有する微量元素によっては、脱脂性能にバラツキを生じる場合があるからである。   In preparing the alkaline electrolyzed water, it is preferable to use “alkaline electrolyzed water having a purity of 99.9% by mass or more”. This is because when “alkaline electrolyzed water having a purity of less than 99.9% by mass” is used, degreasing performance may vary depending on trace elements contained in water.

被洗浄対象物: 本件発明でいう被洗浄対象物は、アルカリ性電解水中に浸漬して、アノード電極との間に電圧を印加することで、カソード電極となる物である限り、特段の限定は無い。従って、被洗浄対象物は、「導電性を有する金属製品」、「少なくとも表面層が導電性を有するプラスチックめっき製品」、「導電性プラスチック製品」等である。そして、これらの被洗浄対象物の形状、サイズ等に関して、特段の限定がないことも、念のために述べておく。 Object to be cleaned: The object to be cleaned in the present invention is not particularly limited as long as it is an object that becomes a cathode electrode by immersing it in alkaline electrolyzed water and applying a voltage to the anode electrode. . Accordingly, the objects to be cleaned are “metal products having conductivity”, “plastic plating products having at least a surface layer having conductivity”, “conductive plastic products”, and the like. It should also be noted that there are no particular limitations on the shape, size, etc. of these objects to be cleaned.

水素バブル: 本件発明においては、アルカリ性電解水中に被洗浄対象物とアノード電極とを配置し、これら被洗浄対象物とアノード電極間に通電することで、被洗浄対象物をカソード分極する被洗浄対象物の表面に水素バブルを形成する。このときの水素バブルは、気泡の直径が20nm〜10μmのマイクロナノバブルであることが好ましい。気泡の直径が20nm未満の場合、その気泡直径を確認することが困難であり、一応の下限値として定めている。一方、気泡の直径が10μmを超えると、被洗浄対象物の表面が、微細な凹凸形状を備える等の場合に、気泡直径が大きすぎて、気泡が凹部に侵入しにくくなるため、十分な電解脱脂効果が得られなくなるため好ましくない。 Hydrogen bubble: In the present invention, an object to be cleaned and an anode electrode are placed in alkaline electrolyzed water, and the object to be cleaned is cathode-polarized by energizing between the object to be cleaned and the anode electrode. Hydrogen bubbles are formed on the surface of the object. The hydrogen bubbles at this time are preferably micro-nano bubbles having a bubble diameter of 20 nm to 10 μm. When the diameter of the bubbles is less than 20 nm, it is difficult to confirm the diameter of the bubbles, and is set as a temporary lower limit value. On the other hand, if the bubble diameter exceeds 10 μm, the surface of the object to be cleaned has a fine uneven shape, etc., and the bubble diameter is too large to make it difficult for the bubbles to enter the recess. This is not preferable because a degreasing effect cannot be obtained.

ここで、「マイクロナノバブル」について述べる。「マイクロナノバブル」は、溶液中に「マイクロバブル」と「ナノバブル」とが混合した状態で、存在することを示すための用語である。「マイクロバブル」とは、一般的に、気泡の直径が、1μm〜10μmの範囲の微細な気泡を指している。そして、「ナノバブル」とは、マイクロバブルに比べて、更に微細な気泡のことであり、一般的には1μm以下のnm単位のものがナノバブルと呼ばれている。このときの気泡は、極めて微細であるため、発生しても肉眼では確認できず、透明な水に見える。   Here, “micro / nano bubbles” will be described. “Micronano bubbles” is a term for indicating that “micro bubbles” and “nano bubbles” are present in a mixed state in a solution. “Microbubble” generally refers to fine bubbles having a diameter of 1 μm to 10 μm. The “nanobubble” is a finer bubble than a microbubble, and generally a nanobubble having a size of 1 μm or less is called a nanobubble. Since the bubbles at this time are extremely fine, even if they are generated, they cannot be confirmed with the naked eye, and appear to be transparent water.

ナノバブルを製造する技術は、未だ完全に確立されておらず、「マイクロバブルを圧壊させて生成する方法」、「SPG(シラスポーラスガラス)膜を用いて生成する方法」、「加圧ガスを、ナノレベルの開口径の穴を備える膜から放出する方法」等が採用されている。これに対し、本件出願にかかる発明の場合、アルカリ性電解水中に、被洗浄対象物とアノード電極とを配置し、当該被洗浄対象物と当該アノード電極間に通電することで、アルカリ性電解水が電解処理され、カソード電極となる被洗浄対象物の表面に、「水素ナノバブル」を含む「マイクロナノバブル」を発生させることが出来る。特に、アルカリ性電解水に、炭酸カリウムが2.8g/L以上、添加されていることで、より効率的に、被洗浄対象物の表面に「水素ナノバブル」を含む「マイクロナノバブル」を発生させることが出来る。   The technology for producing nanobubbles has not been completely established yet, “a method of generating by crushing microbubbles”, “a method of generating using SPG (shirasu porous glass) film”, “pressurized gas, A method of releasing from a film having a hole with a nano-level opening diameter is employed. On the other hand, in the case of the invention according to the present application, the alkaline electrolyzed water is electrolyzed by arranging the object to be cleaned and the anode electrode in the alkaline electrolyzed water and energizing the object to be cleaned and the anode electrode. “Micro-nano bubbles” including “hydrogen nano-bubbles” can be generated on the surface of the object to be cleaned which is treated and becomes a cathode electrode. In particular, by adding 2.8 g / L or more of potassium carbonate to alkaline electrolyzed water, more efficiently generating “micronanobubbles” including “hydrogen nanobubbles” on the surface of the object to be cleaned. I can do it.

更に、この炭酸カリウムに加えて水酸化カリウムをアルカリ性電解水に添加して用いることが好ましい。炭酸カリウムと水酸化カリウムを組み合わせて、これらの濃度が合計して、2.8g/l〜5.6g/l〜となるようにアルカリ性電解水に添加することが好ましい。炭酸カリウム及び水酸化カリウムの合計濃度が2.8g/l未満の場合には、当該炭酸カリウム及び水酸化カリウムを添加することによる水素のマイクロナノバブル発生効率の一定以上の効果を奏することができない。一方、炭酸カリウム及び水酸化カリウムの合計濃度が5.6g/lを超えた場合には、水素のマイクロナノバブルの発生効果は飽和し、薬剤の無駄となるため好ましくない。   Furthermore, it is preferable to add potassium hydroxide to alkaline electrolyzed water in addition to this potassium carbonate. It is preferable that potassium carbonate and potassium hydroxide are combined and added to the alkaline electrolyzed water so that the total concentration thereof is 2.8 g / l to 5.6 g / l. When the total concentration of potassium carbonate and potassium hydroxide is less than 2.8 g / l, it is not possible to achieve a certain effect of hydrogen micro-nano bubble generation efficiency by adding the potassium carbonate and potassium hydroxide. On the other hand, when the total concentration of potassium carbonate and potassium hydroxide exceeds 5.6 g / l, the generation effect of hydrogen micro-nano bubbles is saturated and the chemical is wasted, which is not preferable.

また、当該電解処理における通電条件は、5000mA/dm〜15000mA/dmの範囲の電流を用いることが好ましい。5000mA/dm未満の電流値の場合、脱脂速度が遅く、工業生産で要求される生産性を満足しないため好ましくない。一方、15000mA/dmを超える電流値を採用すると、被洗浄対象物の表面に、凹凸が存在すると、凸部に対する電流集中が顕著となり、被洗浄対象物の表面を均一に電解脱脂することが困難となるため好ましくない。 Further, current conditions in the electrolysis process, it is preferable to use a current in the range of 5000mA / dm 2 ~15000mA / dm 2 . In the case of a current value of less than 5000 mA / dm 2 , the degreasing speed is slow and the productivity required in industrial production is not satisfied, which is not preferable. On the other hand, when a current value exceeding 15000 mA / dm 2 is adopted, if unevenness is present on the surface of the object to be cleaned, current concentration on the convex part becomes remarkable, and the surface of the object to be cleaned can be electrolytically degreased uniformly. Since it becomes difficult, it is not preferable.

更に、当該電解処理の処理時間は、3秒〜5秒の範囲であることが好ましい。ここで、当該電解処理の処理時間が3秒未満の場合、十分に被洗浄対象物の表面の電解脱脂処理をすることが、困難となるため、好ましくない。一方、当該電解処理の処理時間が5秒を超える場合では、電解脱脂能力が飽和するため、処理効率を考慮すると好ましくない。   Furthermore, the treatment time of the electrolytic treatment is preferably in the range of 3 seconds to 5 seconds. Here, when the treatment time of the electrolytic treatment is less than 3 seconds, it is difficult to sufficiently perform electrolytic degreasing treatment on the surface of the object to be cleaned, which is not preferable. On the other hand, when the treatment time of the electrolytic treatment exceeds 5 seconds, the electrolytic degreasing ability is saturated, which is not preferable in view of the treatment efficiency.

キャビテーション現象の発生: 本件発明の場合、上述の水素バブルを破壊することで、被洗浄対象物の表面近傍で水素バブルの破壊に伴うキャビテーション現象を発生させ、被洗浄対象物の表面に付着した汚染物除去を行う。最初に、「水素バブルの破壊」を行う方法に関して述べる。上述のようにマイクロナノバブルの状態の水素バブルの場合、「ナノバブル」に相当する気泡は、衝撃を加える等の外部要因が無い限り、そのままでは消失しない。そこで、被洗浄対象物の表面近傍にある当該水素バブルに対して、アルカリ性電解水中で超音波を照射することにより、「水素バブルの破壊」を行うことが好ましい。 Occurrence of cavitation phenomenon: In the case of the present invention, by destroying the above-mentioned hydrogen bubbles, a cavitation phenomenon accompanying the destruction of hydrogen bubbles occurs near the surface of the object to be cleaned, and the contamination adhered to the surface of the object to be cleaned Remove objects. First, a method for “destruction of hydrogen bubbles” will be described. As described above, in the case of hydrogen bubbles in a micro-nano bubble state, bubbles corresponding to “nano bubbles” do not disappear as they are unless there is an external factor such as an impact. Therefore, it is preferable to perform “destruction of hydrogen bubbles” by irradiating the hydrogen bubbles in the vicinity of the surface of the object to be cleaned with ultrasonic waves in alkaline electrolyzed water.

水素バブルの破壊が起こると、その破壊時の衝撃波により、被洗浄対象物の表面にある油分等の汚染物質の除去効率が飛躍的に高まる。このキャビテーション現象における水素バブルの破壊の衝撃波を用いることにより、被洗浄対象物の形状、被洗浄対象物の表面性状が、どのようなものであっても、効率良く汚染物質の除去が可能となる。   When a hydrogen bubble breaks down, the removal efficiency of contaminants such as oil on the surface of the object to be cleaned increases dramatically due to the shock wave at the time of the break. By using the shock wave of hydrogen bubble destruction in this cavitation phenomenon, it becomes possible to efficiently remove contaminants regardless of the shape of the object to be cleaned and the surface properties of the object to be cleaned. .

アノード電極: 本件出願にかかる電解脱脂方法において、上述のアノード電極は、その表面に10g/m〜20g/mの量の酸化イリジウムを含有する電極触媒層を有する。ここで、本件出願のアノード電極は、その表面に10g/m〜20g/mの量の酸化イリジウムを含有する電極触媒層を有することで、耐久性の向上が図られ、当該電解脱脂効果を長期間安定的に実現させることができる。本件出願のアノード電極は、酸化イリジウムを主成分とする酸化イリジウム電極を用いることで、以下に述べる水素バブルの発生及び油分の分解を容易とし、優れた電解脱脂効果を実現させる。 Anode: in an electrolytic degreasing method according to the present application, the anode electrode of the above, has an electrode catalyst layer containing iridium oxide in an amount of 10g / m 2 ~20g / m 2 on its surface. Here, the anode electrode of the present application, by having the electrode catalyst layer containing iridium oxide in an amount of 10g / m 2 ~20g / m 2 on the surface thereof, improvement of durability is achieved, the electrolytic degreasing effect Can be realized stably for a long period of time. The anode electrode of the present application uses an iridium oxide electrode containing iridium oxide as a main component, thereby facilitating generation of hydrogen bubbles and decomposition of oil as described below, and realizing an excellent electrolytic degreasing effect.

この酸化イリジウム電極をアノード電極として用いると、酸化イリジウム電極の表面で酸化作用を備えた「スーパーオキシドアニオン(活性酸素)」を効率よく発生させることが出来る。この「スーパーオキシドアニオン(活性酸素)」は、被洗浄対象物から除去した油分を酸化して、「炭素」と「二酸化炭素」とに分解する。この結果、アルカリ性電解水中に浮遊した油分が消失し、除去した油分の被洗浄対象物表面への再付着が起こらなくなる。なお、このとき「炭素」は、アルカリ性電解水中で沈殿するため、アルカリ性電解水を循環濾過して、清浄な状態を維持することが好ましい。   When this iridium oxide electrode is used as an anode electrode, “superoxide anion (active oxygen)” having an oxidizing action can be efficiently generated on the surface of the iridium oxide electrode. This “superoxide anion (active oxygen)” oxidizes the oil removed from the object to be cleaned and decomposes it into “carbon” and “carbon dioxide”. As a result, the oil component floating in the alkaline electrolyzed water disappears, and the removed oil component does not reattach to the surface of the object to be cleaned. At this time, since “carbon” is precipitated in alkaline electrolyzed water, it is preferable to circulate and filter the alkaline electrolyzed water to maintain a clean state.

<本件出願にかかる電解脱脂装置について>
本件出願にかかる電解脱脂装置は、上述の電解脱脂方法を用いて被洗浄対象物を清浄化するための電解脱脂装置であって、アルカリ性電解水を貯液する脱脂槽と、当該脱脂槽内に配置するアノード電極と、当該被洗浄対象物をアルカリ性電解水中に浸漬した状態で配置してカソード分極するための通電手段と、当該被洗浄対象物の表面近傍での水素バブルの破壊手段とを備えるものである。そして、本件出願にかかる電解脱脂装置において、当該循環濾過手段は、当該脱脂槽からオーバーフローした当該アルカリ性電解水を濾過手段により濾過した後に当該脱脂槽の下部へ返送するものであることを特徴とする。以下、本件出願にかかる電解脱脂装置について、図を用いて具体的に説明する。
<About the electrolytic degreasing apparatus according to the present application>
The electrolytic degreasing apparatus according to the present application is an electrolytic degreasing apparatus for cleaning an object to be cleaned using the electrolytic degreasing method described above, and a degreasing tank for storing alkaline electrolyzed water, and the degreasing tank. An anode electrode to be disposed; a current-carrying means for placing the object to be cleaned immersed in alkaline electrolyzed water and cathodic polarization; and a means for destroying a hydrogen bubble near the surface of the object to be cleaned Is. And in the electrolytic degreasing apparatus according to the present application, the circulation filtering means returns the alkaline electrolyzed water overflowed from the degreasing tank to the lower part of the degreasing tank after being filtered by the filtering means. . Hereinafter, the electrolytic degreasing apparatus according to the present application will be specifically described with reference to the drawings.

図1には、電解脱脂装置の一実施形態における概略説明図を示す。本実施の形態における被洗浄対象物は、油分等の汚染物質が表面に残存した圧延鋼帯20である。本件発明を採用した電解脱脂装置1は、アルカリ性電解水を貯液する脱脂槽10と、当該アルカリ性電解水中に浸漬されるアノード電極11、11と、通電手段としての整流器12と、アルカリ性電解水中に浸漬される圧延鋼帯20の表面近傍の水素バブルの破壊手段としての超音波照射装置(超音波照射手段)13とを備える。   In FIG. 1, the schematic explanatory drawing in one Embodiment of an electrolytic degreasing apparatus is shown. The object to be cleaned in the present embodiment is a rolled steel strip 20 on which contaminants such as oil remain on the surface. An electrolytic degreasing apparatus 1 employing the present invention includes a degreasing tank 10 for storing alkaline electrolyzed water, anode electrodes 11 and 11 immersed in the alkaline electrolyzed water, a rectifier 12 as an energizing means, and alkaline electrolyzed water. An ultrasonic irradiation device (ultrasonic irradiation means) 13 is provided as a hydrogen bubble destruction means in the vicinity of the surface of the rolled steel strip 20 to be immersed.

脱脂槽10内には、アルカリ性電解水を貯留する。本実施の形態におけるアルカリ性電解水は、一般的にアルカリ性電解水を生成するために用いる電解水生成装置を採用する。また、当該アルカリ性電解水には、電解水生成時から少なくとも48時間以内のものを用い、当該アルカリ性電解水には、炭酸カリウム及び水酸化カリウムを所定濃度となるように添加する。   In the degreasing tank 10, alkaline electrolyzed water is stored. The alkaline electrolyzed water in the present embodiment generally employs an electrolyzed water generating device that is used to generate alkaline electrolyzed water. Further, as the alkaline electrolyzed water, water used within at least 48 hours from the time of electrolyzed water generation is used, and potassium carbonate and potassium hydroxide are added to the alkaline electrolyzed water so as to have predetermined concentrations.

アノード電極11は、少なくとも2つの電極を所定の寸法をおいて対向してアルカリ性電解水中に浸漬した状態で配置して用いる。このとき、本実施の形態では、各アノード電極11、11をほぼ平行に対向させて配置している。各アノード電極11、11は、上述した電解脱脂方法の場合と同様に、酸化イリジウムを主成分とする酸化イリジウム電極を用いることが好ましく、その表面に10g/m〜20g/mの量の酸化イリジウムを含有する電極触媒層を有することがより好ましい。 The anode electrode 11 is arranged and used in a state where at least two electrodes are opposed to each other with a predetermined dimension and are immersed in alkaline electrolyzed water. At this time, in the present embodiment, the anode electrodes 11 are arranged so as to face each other substantially in parallel. Each anode electrode 11 and 11, as in the case of electrolytic degreasing method described above, it is preferable to use the iridium oxide electrode mainly composed of iridium oxide in an amount of 10g / m 2 ~20g / m 2 on its surface It is more preferable to have an electrode catalyst layer containing iridium oxide.

また、本件出願にかかる電解脱脂装置において、脱脂槽10は、少なくとも内面を超音波を反射可能な材質で形成し、アノード電極11は、超音波を透過可能とする連通部を備えたことが好ましい。ここで、アノード電極11は、連通部を備えることで、このアノード電極11によって超音波の進路が妨害されずに脱脂槽10内を反射し、圧延鋼帯20の表面近傍にある水素バブルの破壊が促進されることとなる。例えば、アノード電極11は、図2に例示するように、メッシュ状に形成して連通部11aを備えたり、板にパンチング孔を形成して連通部11aを備えたものとすることで、超音波の透過率が高められ好ましい。特に、本件発明において、アノード電極11は、ラス網で形成して連通部11aを備えることで、超音波の透過率が更に高められることとなるため、より好ましい。また、脱脂槽10の内面をステンレス鋼製とすることで、アルカリ性電解水中で照射された超音波の増幅が効果的に図られ、被洗浄対象物の表面近傍にある水素バブルの破壊がより促進されることとなる。   Moreover, in the electrolytic degreasing apparatus according to the present application, it is preferable that the degreasing tank 10 includes at least an inner surface made of a material that can reflect ultrasonic waves, and the anode electrode 11 includes a communication portion that can transmit ultrasonic waves. . Here, the anode electrode 11 is provided with a communication part, so that the anode electrode 11 reflects the inside of the degreasing tank 10 without obstructing the path of the ultrasonic wave, and the hydrogen bubbles near the surface of the rolled steel strip 20 are destroyed. Will be promoted. For example, as illustrated in FIG. 2, the anode electrode 11 is formed in a mesh shape and includes a communication portion 11 a, or a punching hole is formed in a plate and includes the communication portion 11 a. This is preferable because the transmittance is increased. In particular, in the present invention, the anode electrode 11 is more preferably formed by a lath net and provided with the communication portion 11a, since the transmittance of ultrasonic waves can be further increased. Further, by making the inner surface of the degreasing tank 10 made of stainless steel, the ultrasonic wave irradiated in the alkaline electrolyzed water is effectively amplified, and the destruction of hydrogen bubbles near the surface of the object to be cleaned is further promoted. Will be.

本実施の形態では、圧延鋼帯20は、走行手段を構成する図示しない操出部と巻取部によって、一方向(操出部側)から他方向(巻取部側)に走行されるものである。操出部から繰り出された圧延鋼帯20は、脱脂槽10のアルカリ性電解水中に配置されるアノード電極11、11との間を走行した後、巻取部にて巻き取られる。そのため、圧延鋼帯20は、アルカリ性電解水中において、対向配置されるアノード電極11、11との間に位置し、それぞれのアノード電極11、11と所定の寸法をおいて配置されることとなる。   In the present embodiment, the rolled steel strip 20 is traveled from one direction (steering portion side) to the other direction (winding portion side) by an unillustrated unreeling portion and winding portion constituting the traveling means. It is. The rolled steel strip 20 fed out from the feeding portion travels between the anode electrodes 11 and 11 disposed in the alkaline electrolyzed water of the degreasing tank 10 and is then wound up by the winding portion. Therefore, the rolled steel strip 20 is positioned between the anode electrodes 11 and 11 facing each other in the alkaline electrolyzed water, and is disposed with a predetermined dimension with each anode electrode 11 and 11.

また、圧延鋼帯20表面の電解脱脂処理時間を十分に確保するため、脱脂槽10は、当該圧延鋼帯20の走行方向に長く構成されることが好ましく、同様に、脱脂槽10内のアルカリ性電解水中に浸漬される各アノード電極11、11も当該圧延鋼帯20の走行方向に長く構成されることが好ましい。図1では、操出部側もしくは、巻取部側からみた概略断面図を示している。   Moreover, in order to ensure sufficient time for electrolytic degreasing treatment on the surface of the rolled steel strip 20, the degreasing tank 10 is preferably configured to be long in the traveling direction of the rolled steel strip 20, and similarly, the alkaline property in the degreased tank 10 is set. Each of the anode electrodes 11 and 11 immersed in the electrolytic water is preferably configured to be long in the traveling direction of the rolled steel strip 20. In FIG. 1, the schematic sectional drawing seen from the operation part side or the winding-up part side is shown.

そして、通電手段としての整流器12によって、各アノード電極11、11には正の電荷が印加され、圧延鋼帯20には負の電荷が印加される。   Then, a positive charge is applied to each anode electrode 11, 11 and a negative charge is applied to the rolled steel strip 20 by the rectifier 12 as the energizing means.

また、この脱脂槽10には、圧延鋼帯20が走行する位置の下方に対応して超音波照射装置13が配設される。この超音波照射装置13は、圧延鋼帯20への通電によって、当該圧延鋼帯20の表面近傍に発生する水素バブルに向けて35Hz〜45Hzの超音波を照射する手段であり、本実施の形態では、出力100Wの装置を採用する。また、本実施の形態では、超音波照射装置13を脱脂槽10の底面に配設しているが、この配設位置は、これに限定されない。負の電荷が印加される圧延鋼帯20の表面近傍に向けて超音波を照射することが可能な位置であれば、いずれの位置であってもよいものとする。   Moreover, in this degreasing tank 10, the ultrasonic irradiation apparatus 13 is arrange | positioned corresponding to the downward direction of the position where the rolled steel strip 20 travels. This ultrasonic irradiation device 13 is means for irradiating the rolled steel strip 20 with ultrasonic waves of 35 Hz to 45 Hz toward hydrogen bubbles generated near the surface of the rolled steel strip 20, and this embodiment Then, an apparatus with an output of 100 W is adopted. Moreover, in this Embodiment, although the ultrasonic irradiation apparatus 13 is arrange | positioned in the bottom face of the degreasing tank 10, this arrangement | positioning position is not limited to this. Any position may be used as long as the ultrasonic wave can be irradiated toward the vicinity of the surface of the rolled steel strip 20 to which a negative charge is applied.

また、図1には、この脱脂槽10に、アルカリ性電解水の循環濾過機構(循環濾過手段)30が備えられているのが示されている。この循環濾過機構30は、少なくとも濾過手段としてのフィルタ31と、当該フィルタ31に脱脂槽10内のアルカリ性電解水を搬送するポンプ32とを有している。本実施の形態では、脱脂槽10内のアルカリ性電解水の水面付近の高さ位置に、脱脂槽10内のアルカリ性電解水を循環濾過するためのアルカリ性電解水回収部16が形成されており、当該アルカリ性電解水回収部16には、循環用配管34が接続されている。この循環用配管34の他端は、フィルタ31に接続されており、当該フィルタ31には循環用配管35を介してポンプ32が接続されている。このポンプ32は、調整槽33に接続されており、当該調整槽33には循環用配管36を介して濾過処理後のアルカリ性電解水を脱脂槽10に返送する循環返送口15が接続されている。なお、本実施の形態においてフィルタ31は、ポリプロピレン製を採用する。   Further, FIG. 1 shows that the degreasing tank 10 is provided with a circulating filtration mechanism (circulating filtration means) 30 for alkaline electrolyzed water. The circulation filtering mechanism 30 includes at least a filter 31 as a filtering unit and a pump 32 that conveys alkaline electrolyzed water in the degreasing tank 10 to the filter 31. In this Embodiment, the alkaline electrolyzed water collection | recovery part 16 for circulating and filtering the alkaline electrolyzed water in the degreasing tank 10 is formed in the height position near the water surface of the alkaline electrolyzed water in the degreasing tank 10, and the said A circulation pipe 34 is connected to the alkaline electrolyzed water recovery unit 16. The other end of the circulation pipe 34 is connected to a filter 31, and a pump 32 is connected to the filter 31 via a circulation pipe 35. The pump 32 is connected to an adjustment tank 33, and a circulation return port 15 for returning the alkaline electrolyzed water after filtration to the degreasing tank 10 is connected to the adjustment tank 33 through a circulation pipe 36. . In the present embodiment, the filter 31 is made of polypropylene.

以上の構成により、本実施の形態にかかる電解脱脂装置1の動作について説明する。まず初めに、走行手段を作動させて、被洗浄対象物である圧延鋼帯20を操出部側から巻取部側に向けて走行させる。そして、整流器12により、アルカリ性電解水中に浸漬された各アノード電極11、11に正の電荷を印加し、圧延鋼帯20に負の電荷を印加する。   With the above configuration, the operation of the electrolytic degreasing apparatus 1 according to the present embodiment will be described. First, the traveling means is operated to cause the rolled steel strip 20 that is the object to be cleaned to travel from the feeding portion side toward the winding portion side. The rectifier 12 applies a positive charge to the anode electrodes 11 and 11 immersed in the alkaline electrolyzed water, and applies a negative charge to the rolled steel strip 20.

これにより、脱脂槽10内のアルカリ性電解水が、電気分解され、カソード電極となる圧延鋼帯20の表面に「水素ナノバブル」を含む「マイクロナノバブル」が発生する。ここで、当該圧延鋼帯20の表面近傍に向けて超音波照射装置13から超音波が照射されている。これにより、圧延鋼帯20の表面近傍に形成された「マイクロナノバブル」を含む「水素バブル」は、超音波により破壊され、当該水素バブルの破壊に伴って、キャビテーション現象が発生し、圧延鋼帯20の表面に付着した汚染物が当該圧延鋼帯20表面から除去される。   Thereby, the alkaline electrolyzed water in the degreasing tank 10 is electrolyzed, and “micro-nano bubbles” including “hydrogen nano-bubbles” are generated on the surface of the rolled steel strip 20 serving as a cathode electrode. Here, ultrasonic waves are irradiated from the ultrasonic irradiation device 13 toward the vicinity of the surface of the rolled steel strip 20. As a result, the “hydrogen bubbles” including “micro-nano bubbles” formed in the vicinity of the surface of the rolled steel strip 20 are broken by ultrasonic waves, and a cavitation phenomenon occurs with the destruction of the hydrogen bubbles, and the rolled steel strip. The contaminant adhering to the surface of 20 is removed from the surface of the rolled steel strip 20.

一方、脱脂槽10内のアルカリ性電解水が電気分解されることで、アノード電極11、11表面から酸素バブルが発生する。このとき、アノード電極は、上述したように酸化イリジウム電極を用いているため、アノード電極11の表面から発生した酸素が分解されて、スーパーオキシドアニオン(活性酸素)が効率的に発生する。アノード電極11の表面近傍において、発生したスーパーオキシドアニオン(活性酸素)は、脱脂槽10内のアルカリ性電解水中に拡散し、圧延鋼帯20表面から分離除去された油分等の汚染物と反応して、当該油分を酸化し、炭素と二酸化炭素に分解する。   On the other hand, when the alkaline electrolyzed water in the degreasing tank 10 is electrolyzed, oxygen bubbles are generated from the surfaces of the anode electrodes 11 and 11. At this time, since the iridium oxide electrode is used as the anode electrode as described above, oxygen generated from the surface of the anode electrode 11 is decomposed and superoxide anions (active oxygen) are efficiently generated. In the vicinity of the surface of the anode 11, the generated superoxide anion (active oxygen) diffuses into the alkaline electrolyzed water in the degreasing tank 10 and reacts with contaminants such as oil separated and removed from the surface of the rolled steel strip 20. The oil is oxidized and decomposed into carbon and carbon dioxide.

分解された二酸化炭素は、ガスとして大気中に放出されて処理される。他方、循環濾過機構30のポンプ32を作動することにより、炭素が含まれたアルカリ性電解水は、脱脂槽10内のアルカリ性電解水の水面付近の高さ位置に形成されたアルカリ性電解水回収部16から循環用配管34を介してフィルタ31に至る。このフィルタ31によって、アルカリ性電解水中の炭素は、吸着除去処理され、炭素が除去されたアルカリ性電解水は、循環用配管35、ポンプ32、調整槽33を介して循環返送口15より脱脂槽10内に返送される。   The decomposed carbon dioxide is released into the atmosphere as a gas and processed. On the other hand, by operating the pump 32 of the circulation filtration mechanism 30, the alkaline electrolyzed water containing carbon is formed in the alkaline electrolyzed water recovery unit 16 formed at a height near the surface of the alkaline electrolyzed water in the degreasing tank 10. To the filter 31 via the circulation pipe 34. The filter 31 adsorbs and removes the carbon in the alkaline electrolyzed water, and the alkaline electrolyzed water from which the carbon has been removed enters the degreasing tank 10 from the circulation return port 15 via the circulation pipe 35, the pump 32, and the adjustment tank 33. Will be returned.

本件発明の電解脱脂装置1によれば、カソード分極する圧延鋼帯20の表面に直径が20nm〜10μmの水素ナノバブルを発生させるため、当該圧延鋼帯20の表面形状が複雑な場合であっても、当該表面形状の凹部にまで直径が20nm〜10μmの水素ナノバブルが侵入させることができる。凹部にまで侵入した水素ナノバブルは、超音波が照射されて、破壊され、当該破壊に伴う衝撃波によって、当該凹部に付着した油分等の汚染物質を効果的に除去することが可能となる。これにより、従来のアルカリ脱脂方法と比べて、格段に優れた清浄化効果を得ることができる。   According to the electrolytic degreasing apparatus 1 of the present invention, hydrogen nanobubbles having a diameter of 20 nm to 10 μm are generated on the surface of the cathode steel-polarized rolled steel strip 20, so that even if the surface shape of the rolled steel strip 20 is complicated. In addition, hydrogen nanobubbles having a diameter of 20 nm to 10 μm can penetrate into the concave portion having the surface shape. The hydrogen nanobubbles that have penetrated into the recesses are destroyed by being irradiated with ultrasonic waves, and the contaminants such as oil adhering to the recesses can be effectively removed by the shock wave accompanying the destruction. Thereby, compared with the conventional alkali degreasing method, the cleaning effect outstandingly excellent can be acquired.

更に、本件発明の電解脱脂装置1によれば、圧延鋼帯20の表面から分離除去された油分等の汚染物質は、アルカリ性電解水の電気分解の際にアノード電極の表面から生成する「スーパーオキシドアニオン(活性酸素)」により酸化され、「炭素」と「二酸化炭素」とに分解される。炭素はアルカリ性電解水中に沈殿するため、本件発明の電解脱脂装置1は、沈殿濾過機構(不図示)を備えていても良い。この場合には、当該沈殿濾過機構による濾過処理によって、沈殿した炭素が除去され、二酸化炭素はアルカリ性電解水中から大気中に放出される。これにより、圧延鋼帯20の表面から分離除去した油分等の汚染物質は、効率的に分解除去されるため、圧延鋼帯20表面への再付着を回避することが出来る。   Furthermore, according to the electrolytic degreasing apparatus 1 of the present invention, contaminants such as oil separated and removed from the surface of the rolled steel strip 20 are generated from the surface of the anode electrode during electrolysis of alkaline electrolyzed water. It is oxidized by “anions (active oxygen)” and decomposed into “carbon” and “carbon dioxide”. Since carbon precipitates in alkaline electrolyzed water, the electrolytic degreasing apparatus 1 of the present invention may include a precipitation filtration mechanism (not shown). In this case, the precipitated carbon is removed by the filtration treatment by the precipitation filtration mechanism, and the carbon dioxide is released from the alkaline electrolyzed water to the atmosphere. Thereby, contaminants such as oil components separated and removed from the surface of the rolled steel strip 20 are efficiently decomposed and removed, so that reattachment to the surface of the rolled steel strip 20 can be avoided.

なお、上述した一実施の形態では、ロール状に巻き取られた長尺形状の圧延鋼帯20を一方向から繰り出し、他方向から巻き取る形態を採用しているが、本件発明における被洗浄対象物はこれに限定されるものではない。例えば、図2に示すように、走行手段を構成する搬送ライン21に所定間隔をおいて複数の吊下部材22を設け、各吊下部材22の下端に被洗浄対象物23を着脱自在に取り付けてもよい。また、本件発明における被洗浄対象物は、これ以外にも、走行手段によって一方向から他方向に走行可能なものであれば、巻き取りが不可能な板状のものであってもよい。   In the above-described embodiment, the long rolled steel strip 20 wound up in a roll shape is taken out from one direction and taken up from the other direction, but the object to be cleaned in the present invention is used. A thing is not limited to this. For example, as shown in FIG. 2, a plurality of suspension members 22 are provided at a predetermined interval on a conveyance line 21 that constitutes a traveling unit, and an object to be cleaned 23 is detachably attached to the lower end of each suspension member 22. May be. In addition, the object to be cleaned in the present invention may be a plate-like object that cannot be wound as long as it can travel from one direction to the other direction by the traveling means.

本件出願にかかる電解脱脂方法によれば、被洗浄対象物の表面を効果的に清浄化処理することができ、その後において行われるめっき皮膜の形成を良好に行うことが可能であり、脱脂処理が要求されるあらゆる製品に適用可能なものである。特に、めっき層を形成しようとする製品の表面の清浄化には好適である。本件出願にかかる電解脱脂方法を用いることで、複雑な微細凹凸を備えるめっき対象物の表面から、効率よく汚染物質を除去し、除去した油分の被洗浄対象物表面への再付着を防止し、良好な品質を備えるめっき層の形成が可能となる。   According to the electrolytic degreasing method according to the present application, it is possible to effectively clean the surface of the object to be cleaned, and it is possible to satisfactorily perform the formation of a plating film performed thereafter. Applicable to all required products. In particular, it is suitable for cleaning the surface of a product for which a plating layer is to be formed. By using the electrolytic degreasing method according to the present application, it is possible to efficiently remove contaminants from the surface of the plating object having complex fine irregularities, and prevent the removed oil from being reattached to the surface of the object to be cleaned. A plating layer having good quality can be formed.

そして、本件出願にかかる電解脱脂装置は、特殊な構造を要するものではなく、装置設計も容易である。また、本件出願にかかる電解脱脂装置は、例えば、めっきライン、真空蒸着ライン等の連続生産ラインに組み込むことも容易であり、被洗浄対象物を連続し、最終製品の製造が可能である。   And the electrolytic degreasing apparatus concerning this application does not require a special structure, and apparatus design is also easy. In addition, the electrolytic degreasing apparatus according to the present application can be easily incorporated into a continuous production line such as a plating line or a vacuum vapor deposition line, and can continuously manufacture an object to be cleaned.

1 電解脱脂装置
10 脱脂槽
11 アノード電極
11a 連通部
12 整流器(通電手段)
13 超音波照射装置(超音波照射手段。水素バブル破壊手段)
15 循環返送口
16 アルカリ性電解水回収部
20 圧延鋼帯(被洗浄対象物)
21 搬送ライン
22 吊下部材
23 被洗浄対象物
30 循環濾過機構(循環濾過手段)
31 フィルタ(濾過手段)
32 ポンプ
33 調整槽
34 循環用配管
35 循環用配管
36 返送用配管
DESCRIPTION OF SYMBOLS 1 Electrolytic degreasing apparatus 10 Degreasing tank 11 Anode electrode 11a Communication part 12 Rectifier (energization means)
13 Ultrasonic irradiation device (ultrasonic irradiation means. Hydrogen bubble destruction means)
15 Circulation return port 16 Alkaline electrolyzed water recovery part 20 Rolled steel strip (object to be cleaned)
21 Conveying line 22 Suspended member 23 Object to be cleaned 30 Circulation filtration mechanism (circulation filtration means)
31 Filter (filtering means)
32 Pump 33 Adjustment tank 34 Circulation piping 35 Circulation piping 36 Return piping

Claims (8)

アルカリ性電解水を用いて被洗浄対象物の表面に付着した油分等の汚染物を除去する脱脂方法であって、
アルカリ性電解水中に被洗浄対象物とアノード電極とを配置し通電することで、被洗浄対象物をカソード分極して、被洗浄対象物の表面に直径20nm〜10μmの水素バブルを形成し、被洗浄対象物の表面近傍で水素バブルを破壊させ、当該破壊に伴う衝撃波により被洗浄対象物の表面に付着した汚染物除去を行うものであり、
当該アノード電極は、その表面に10g/m〜20g/mの量の酸化イリジウムを含有する電極触媒層を有することを特徴とする電解脱脂方法。
A degreasing method for removing contaminants such as oil adhering to the surface of an object to be cleaned using alkaline electrolyzed water,
The object to be cleaned and the anode electrode are placed in the alkaline electrolyzed water and energized to cathodically polarize the object to be cleaned to form hydrogen bubbles with a diameter of 20 nm to 10 μm on the surface of the object to be cleaned. The hydrogen bubble is destroyed near the surface of the object, and the contaminants attached to the surface of the object to be cleaned are removed by the shock wave accompanying the destruction.
The anode electrode, electrolytic degreasing method characterized by having an electrode catalyst layer containing iridium oxide in an amount of 10g / m 2 ~20g / m 2 on its surface.
前記アルカリ性電解水は、炭酸カリウム及び水酸化カリウムを含むpH11〜pH13の水溶液を用いる請求項1に記載の電解脱脂方法。   The electrolytic degreasing method according to claim 1, wherein the alkaline electrolyzed water uses an aqueous solution of pH 11 to pH 13 containing potassium carbonate and potassium hydroxide. 被洗浄対象物の表面近傍での水素バブルの破壊は、当該水素バブルに対して、アルカリ性電解水中で超音波を照射することにより行う請求項1又は請求項2に記載の電解脱脂方法。   The electrolytic degreasing method according to claim 1 or 2, wherein the hydrogen bubbles near the surface of the object to be cleaned are destroyed by irradiating the hydrogen bubbles with ultrasonic waves in alkaline electrolyzed water. 通電中の前記アノード電極で発生したスーパーオキシドアニオンと、前記被洗浄対象物の表面から除去した油分とを、前記アルカリ性電解水中で反応させ、当該油分を炭素と二酸化炭素とに分解する請求項1〜請求項3のいずれかに記載の電解脱脂方法。   The superoxide anion generated at the anode electrode being energized and the oil removed from the surface of the object to be cleaned are reacted in the alkaline electrolyzed water to decompose the oil into carbon and carbon dioxide. The electrolytic degreasing method according to claim 3. 請求項1〜請求項4のいずれかに記載の脱脂方法を用いて被洗浄対象物の表面を清浄化するための電解脱脂装置であって、
アルカリ性電解水を貯液する脱脂槽と、
当該脱脂槽内に配置するアノード電極と、
当該アルカリ性電解水中に前記被洗浄対象物を浸漬した状態で配置し、当該被洗浄対象物をカソード分極して当該被洗浄対象物の表面に直径20nm〜10μmの水素バブルを形成するための通電手段と、
当該被洗浄対象物の表面近傍の水素バブルを破壊する水素バブル破壊手段と、
当該アルカリ性電解水の循環濾過手段とを備え、
当該循環濾過手段は、当該脱脂槽からオーバーフローした当該アルカリ性電解水を濾過手段により濾過した後に当該脱脂槽の下部へ返送するものであることを特徴とする電解脱脂装置。
An electrolytic degreasing apparatus for cleaning the surface of an object to be cleaned using the degreasing method according to claim 1,
A degreasing tank for storing alkaline electrolyzed water;
An anode electrode disposed in the degreasing tank;
An energization means for disposing the object to be cleaned in the alkaline electrolyzed water and cathodicly polarizing the object to be cleaned to form hydrogen bubbles having a diameter of 20 nm to 10 μm on the surface of the object to be cleaned. When,
Hydrogen bubble destruction means for destroying hydrogen bubbles near the surface of the object to be cleaned;
A circulating filtration means for the alkaline electrolyzed water,
The electrolytic degreasing apparatus characterized in that the circulation filtering means returns the alkaline electrolyzed water overflowed from the degreasing tank to the lower part of the degreasing tank after being filtered by the filtering means.
前記アノード電極には、酸化イリジウム電極を用いる請求項5に記載の電解脱脂装置。   The electrolytic degreasing apparatus according to claim 5, wherein an iridium oxide electrode is used as the anode electrode. 前記脱脂槽は、少なくとも内面を超音波を反射可能な材質で形成し、前記アノード電極は、超音波を透過可能とする連通部を備えた請求項5又は請求項6に記載の電解脱脂装置。   The electrolytic degreasing apparatus according to claim 5 or 6, wherein at least an inner surface of the degreasing tank is formed of a material capable of reflecting ultrasonic waves, and the anode electrode includes a communication portion that allows ultrasonic waves to pass therethrough. 前記水素バブル破壊手段は、被洗浄対象物の表面で発生する水素バブルに対して、アルカリ性電解水中で超音波を照射する超音波照射手段である請求項5〜請求項7のいずれかに記載の電解脱脂装置。   The said hydrogen bubble destruction means is an ultrasonic irradiation means which irradiates an ultrasonic wave in alkaline electrolyzed water with respect to the hydrogen bubble generate | occur | produced on the surface of a to-be-cleaned target object. Electrolytic degreasing equipment.
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