TW201900935A - Electrogalvanizing device and electroplating method - Google Patents

Electrogalvanizing device and electroplating method Download PDF

Info

Publication number
TW201900935A
TW201900935A TW107116234A TW107116234A TW201900935A TW 201900935 A TW201900935 A TW 201900935A TW 107116234 A TW107116234 A TW 107116234A TW 107116234 A TW107116234 A TW 107116234A TW 201900935 A TW201900935 A TW 201900935A
Authority
TW
Taiwan
Prior art keywords
water
plated
treatment
tank
washing
Prior art date
Application number
TW107116234A
Other languages
Chinese (zh)
Other versions
TWI750374B (en
Inventor
津村豊光
Original Assignee
日商日本拉斯派特股份有限公司
日商西田製作所股份有限公司
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 日商日本拉斯派特股份有限公司, 日商西田製作所股份有限公司 filed Critical 日商日本拉斯派特股份有限公司
Publication of TW201900935A publication Critical patent/TW201900935A/en
Application granted granted Critical
Publication of TWI750374B publication Critical patent/TWI750374B/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/02Electroplating: Baths therefor from solutions
    • C25D3/22Electroplating: Baths therefor from solutions of zinc
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D17/00Constructional parts, or assemblies thereof, of cells for electrolytic coating
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D21/00Processes for servicing or operating cells for electrolytic coating
    • C25D21/12Process control or regulation
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D21/00Processes for servicing or operating cells for electrolytic coating
    • C25D21/16Regeneration of process solutions
    • C25D21/20Regeneration of process solutions of rinse-solutions
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/34Pretreatment of metallic surfaces to be electroplated
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Automation & Control Theory (AREA)
  • Electroplating Methods And Accessories (AREA)

Abstract

Provided is an electrogalvanizing apparatus, which is possible to greatly reduce the amount of water used for washing a product to be plated. An electrogalvanizing apparatus (1) for performing a treatment of forming a galvanized coating on a surface of the product to be plated includes: a pretreatment unit (2) that performs a degreasing treatment on a surface of the product to be plated and a bottom layer adjustment; and a plating treatment unit (3) for performing a plating treatment by using plating solution on a surface of the product to be plated which has been subjected to a degreasing treatment and a bottom layer adjustment; the pretreatment unit (2) performs bottom layer adjustment of the surface of the product to be plated by spraying an abrasive onto the surface of the product to be plated.

Description

電鍍鋅裝置及電鍍鋅方法Galvanizing device and galvanizing method

本發明是關於用於在被鍍品的表面形成鍍鋅被膜之電鍍鋅裝置及電鍍鋅方法的技術。The present invention relates to a technology of an electro-galvanizing device and an electro-galvanizing method for forming a galvanized coating on a surface of an article to be plated.

以往,進行在被鍍品的表面形成鍍鋅被膜或鍍鋅合金被膜的處理之電鍍鋅裝置及電鍍鋅方法的相關技術,是已知的(參照專利文獻1)。   前述電鍍鋅裝置係具備前處理部及電鍍處理部。Conventionally, technologies related to an electrogalvanizing apparatus and an electrogalvanizing method for forming a galvanized coating or a galvanized alloy coating on the surface of a to-be-plated product are known (see Patent Document 1). The aforementioned galvanizing apparatus includes a pre-treatment section and a plating treatment section.

在前述電鍍鋅裝置中,前處理部係進行:利用鹼性脫脂等來將被鍍品之表面的油脂去除的處理(脫脂處理)、以及利用鹽酸等的酸洗淨或電解脫脂等來將被鍍品之表面的氧化物去除的處理(底層調整)等。   此外,在前述電鍍鋅裝置中,電鍍處理部是例如由滾筒式電鍍鋅裝置構成,在將被實施脫脂處理以及底層調整後之被鍍品收納於滾筒內的狀態下,對該被鍍品之表面使用電鍍液進行電鍍處理。In the aforementioned electro-galvanizing apparatus, the pre-treatment section performs a treatment (degreasing treatment) for removing grease on the surface of the plated product by alkaline degreasing, etc., and an acid-washing or electrolytic degreasing process using hydrochloric acid or the like Treatment of oxide removal on the surface of the plated product (bottom layer adjustment), etc. Further, in the aforementioned electrogalvanizing apparatus, the electroplating treatment section is constituted by, for example, a drum-type electrogalvanizing apparatus, and in a state where the to-be-plated product subjected to degreasing treatment and bottom layer adjustment is stored in a drum, the The surface is plated with a plating solution.

[專利文獻1] 日本特開2002-4080號公報[Patent Document 1] Japanese Patent Laid-Open No. 2002-4080

[發明所欲解決之問題][Problems to be solved by the invention]

然而,在前述電鍍鋅裝置之前處理部中,於脫脂處置、底層調整等之後必須分別進行將被鍍品水洗的處理。   如此般,在前述電鍍鋅裝置,在前處理部中,當進行將被鍍品之表面的油脂或氧化物等去除的處理時,存在著將被鍍品洗淨的水需要大量、排水大量(例如,每一小時數百公升)產生的問題。However, in the pre-treatment section of the aforementioned electro-galvanizing device, after the degreasing treatment, the adjustment of the bottom layer, and the like, it is necessary to separately perform the treatment of washing the plated product with water. As described above, in the aforementioned electro-galvanizing device, in the pre-treatment section, when a treatment is performed to remove grease, oxides, and the like on the surface of the plated product, there is a large amount of water for washing the plated product and a large amount of drainage ( For example, hundreds of liters per hour).

本發明是有鑑於以上狀況而開發完成的,其目的是為了提供一種電鍍鋅裝置,能夠將在被鍍品的水洗中所使用的水之排水量大幅減少。 [解決問題之技術手段]The present invention has been developed in view of the above circumstances, and an object thereof is to provide a galvanized device capable of greatly reducing the drainage amount of water used in the washing of a plated product. [Technical means to solve the problem]

本發明所欲解決的問題是如以上所述般,接下來說明用於解決該問題之手段。The problem to be solved by the present invention is as described above, and the means for solving the problem will be described next.

亦即,請求項1之電鍍鋅裝置,係進行在被鍍品的表面形成鍍鋅被膜的處理之電鍍鋅裝置,其具備有:進行前述被鍍品的表面之脫脂處理和底層調整之前處理部、以及對被實施前述脫脂處理及前述底層調整後之被鍍品的表面使用電鍍液進行電鍍處理之電鍍處理部,前述前處理部,是藉由對前述被鍍品的表面噴射研磨劑,來進行前述被鍍品的表面之底層調整。That is, the electrogalvanizing apparatus of claim 1 is an electrogalvanizing apparatus that performs a process of forming a galvanized coating on the surface of the object to be plated, and includes a degreasing process for the surface of the object to be plated and a pre-treatment unit for adjusting the bottom layer And an electroplating treatment section for applying a plating solution to the surface of the object to be plated after performing the degreasing treatment and the bottom layer adjustment, the pretreatment portion is made by spraying an abrasive on the surface of the object to be plated. The bottom layer adjustment of the surface of the plated product is performed.

在請求項2中,前述前處理部是使用既定的溶劑來進行前述被鍍品的表面之脫脂處理。In claim 2, the pre-processing section performs a degreasing treatment on the surface of the object to be plated using a predetermined solvent.

在請求項3中,前述前處理部是藉由使用有機溶劑將前述被鍍品的表面之油脂溶解來進行脫脂處理。In claim 3, the pre-processing unit performs a degreasing treatment by dissolving the grease on the surface of the object to be plated with an organic solvent.

在請求項4中,係具備水處理部,該水處理部,是讓在前述電鍍處理部在被鍍品的洗淨中所使用的水分離成水和廢棄物,將該分離後的水作為用於洗淨前述被鍍品的水而供給到前述電鍍處理部。In claim 4, a water treatment unit is provided. The water treatment unit is configured to separate the water used for washing the plated product in the plating treatment unit into water and waste, and use the separated water as Water for washing the object to be plated is supplied to the plating treatment section.

請求項5之電鍍鋅方法,係進行在被鍍品的表面形成鍍鋅被膜的處理之電鍍鋅方法,其具備:進行前述被鍍品的表面之脫脂處理的工序、進行前述被鍍品的表面之底層調整的工序、以及對被實施前述脫脂處理及前述底層調整後之被鍍品的表面使用電鍍液進行電鍍處理的工序,進行前述被鍍品的表面之底層調整的工序,是藉由對被實施前述脫脂處理後之被鍍品的表面噴射研磨劑,來進行前述被鍍品的表面之底層調整。The electrogalvanizing method of claim 5 is a galvanizing method for forming a galvanized coating on the surface of the object to be plated, and includes a step of performing a degreasing treatment on the surface of the object to be plated, and a surface of the object to be plated. The step of adjusting the bottom layer and the step of performing an electroplating treatment on the surface of the plated product subjected to the aforementioned degreasing treatment and the adjustment of the bottom layer using a plating solution. The step of adjusting the bottom layer of the surface of the plated product is performed by An abrasive is sprayed on the surface of the object to be plated after the degreasing treatment is performed to adjust the bottom layer of the surface of the object to be plated.

在請求項6中,進行前述被鍍品的表面之脫脂處理的工序,是使用既定的溶劑來進行前述被鍍品的表面之脫脂處理。 [發明之效果]In claim 6, the step of performing a degreasing treatment on the surface of the plated product is performing a degreasing treatment on the surface of the plated product using a predetermined solvent. [Effect of the invention]

作為本發明的效果,可發揮以下所示般的效果。   亦即,依據本發明,能夠將在被鍍品的水洗中所使用的水之排水量大幅減少。As the effects of the present invention, the following effects can be exhibited. That is, according to the present invention, it is possible to greatly reduce the drainage amount of water used in washing the object to be plated.

接下來,針對本發明的實施形態之電鍍鋅裝置1以及電鍍鋅方法,使用圖1至圖4做說明。Next, the galvanizing apparatus 1 and the galvanizing method according to the embodiments of the present invention will be described with reference to FIGS. 1 to 4.

電鍍鋅裝置1(電鍍鋅方法),是進行在被鍍品的表面形成鍍鋅被膜之處理。在電鍍鋅裝置1(電鍍鋅方法),作為在被鍍品的表面形成鍍鋅被膜之處理,並不限定為利用鋅來在被鍍品的表面形成鍍鋅被膜之處理,也包含利用鋅合金來在被鍍品的表面形成鍍鋅被膜(鍍鋅合金被膜)之處理。   被鍍品是由含有鐵之金屬材所構成之既定構件。藉由電鍍鋅裝置1來形成鍍鋅被膜之被鍍品是包括建築用金屬構件(例如,建築用的金屬製螺釘、或建築用的金屬製接合構件等)。   如圖1所示般,電鍍鋅裝置1係具備:前處理部2、電鍍處理部3、後處理部4、水處理部5、以及中間坑(pit)6。The galvanizing apparatus 1 (galvanizing method) is a process for forming a galvanized film on the surface of an object to be plated. In the galvanizing apparatus 1 (galvanizing method), the process of forming a galvanized film on the surface of the object to be plated is not limited to the process of forming a galvanized film on the surface of the object to be plated with zinc, and also includes the use of a zinc alloy A process of forming a galvanized coating (galvanized alloy coating) on the surface of the object to be plated. The product to be plated is a predetermined member made of a metal material containing iron. The articles to be galvanized by the galvanizing apparatus 1 include metal members for construction (for example, metal screws for construction, or metal joint members for construction). As shown in FIG. 1, the galvanizing apparatus 1 includes a pre-treatment section 2, a plating treatment section 3, a post-treatment section 4, a water treatment section 5, and an intermediate pit 6.

前處理部2係進行將被鍍品的表面之油脂以及氧化物等去除之脫脂處理和底層調整。   在前處理部2中實施處理前之被鍍品(例如,進貨到電鍍工廠的被鍍品)的表面,形成有氧化物(氧化被膜),此外附著有鏽等。此外,在前處理部2中實施處理前之被鍍品的表面,塗布有用於潤滑、防鏽之油脂。   前處理部2係具備脫脂處理部7及底層調整部8。The pre-treatment section 2 performs a degreasing treatment and a bottom layer adjustment for removing grease and oxides on the surface of the article to be plated.氧化物 An oxide (oxidized film) is formed on the surface of the object to be plated (for example, an object to be plated in a plating factory) before the pretreatment is performed in the pretreatment unit 2, and rust and the like are attached. In addition, the surface of the article to be plated before the treatment is performed in the pretreatment section 2 is coated with grease for lubrication and rust prevention. The pre-processing unit 2 includes a degreasing processing unit 7 and a bottom layer adjusting unit 8.

前處理部2之脫脂處理部7,是進行使用既定的溶劑將被鍍品的表面之油脂去除的處理(脫脂處理)。脫脂處理部7是一種非水系脫脂裝置,是藉由使用有機溶劑將被鍍品的表面之油脂溶解來進行脫脂處理。在脫脂處理部7中所使用的有機溶劑,例如包含:二氯甲烷、三氯乙烯、四氯乙烯等的氯系溶劑,或是其他公知的烴系、酯系、醇系、氟系、溴系的溶劑等。The degreasing treatment section 7 of the pretreatment section 2 is a treatment (degreasing treatment) for removing grease from the surface of the object to be plated using a predetermined solvent. The degreasing treatment section 7 is a non-aqueous degreasing device, and performs degreasing treatment by dissolving fats and oils on the surface of the object to be plated with an organic solvent. The organic solvent used in the degreasing treatment section 7 includes, for example, a chlorine-based solvent such as methylene chloride, trichloroethylene, tetrachloroethylene, or other known hydrocarbon-based, ester-based, alcohol-based, fluorine-based, bromine Solvent.

前處理部2之底層調整部8,是進行被實施脫脂處理後之被鍍品的表面之底層調整。底層調整部8是一種噴擊裝置(例如,噴砂裝置、珠擊裝置等),係噴射由二氧化矽、氧化鋁、鋼球、或鋼砂(steel grit)等所構成的研磨劑,將被鍍品的表面之氧化物、鏽等去除,藉此進行被鍍品的表面之底層調整。The bottom layer adjustment section 8 of the pre-processing section 2 performs the bottom layer adjustment of the surface of the object to be plated after the degreasing treatment is performed. The bottom layer adjusting portion 8 is a shot blasting device (for example, a sand blasting device, a bead blasting device, etc.), which sprays abrasives composed of silicon dioxide, alumina, steel balls, or steel grit, etc. The oxide and rust on the surface of the plated product are removed to adjust the bottom layer of the surface of the plated product.

電鍍處理部3,是對在前處理部2中被實施脫脂處理及底層調整後之被鍍品的表面,使用電鍍液進行電鍍處理。   電鍍液,是例如由添加有光澤劑、氯化銨、氯化鉀及氯化鋅等而成者所構成。   電鍍處理部3係一種滾筒式電鍍鋅裝置,且具備有:上游槽10、電鍍槽11、回收槽12及水洗槽13。電鍍處理部3,每經過既定的時間,依上游槽10、電鍍槽11、回收槽12、水洗槽13的順序讓收納有被鍍品之滾筒從上游側往下游側移動,而在各槽內進行各種處理。The plating treatment section 3 performs a plating treatment on a surface of a to-be-plated product subjected to degreasing treatment and underlayer adjustment in the pretreatment section 2 using a plating solution. The hafnium plating solution is made of, for example, a glossing agent, ammonium chloride, potassium chloride, zinc chloride, or the like. The electroplating treatment section 3 is a drum-type galvanizing device, and includes an upstream tank 10, a plating tank 11, a recovery tank 12, and a water washing tank 13. The plating processing unit 3 moves the rollers containing the articles to be plated from the upstream side to the downstream side in the order of the upstream tank 10, the plating tank 11, the recovery tank 12, and the water washing tank 13 in each order in a predetermined time. Perform various processing.

電鍍處理部3之上游槽10,是將在被鍍品(在前處理部2中將油脂以及氧化物等除去後的被鍍品)的表面上所附著的塵垢,用水洗淨。上游槽10,是由供蓄水之複數個(二個)槽所構成。   當滾筒從上游側往下游側移動而位於各上游槽10的上方時,會往下方移動而配置在上游槽10內。而且,在配置於上游槽10內的狀態下讓滾筒旋轉,藉此將滾筒內的被鍍品用水洗淨。   上游槽10也能由一個槽構成。   此外,上游槽10亦可構成為,不是將被鍍品用水洗淨,而是用稀鹽酸或稀硝酸等的表面活性劑將被鍍品的表面進行處理。   此外,上游槽10亦可構成為,用水將被鍍品洗淨後,用表面活性劑將被鍍品的表面進行處理。The upstream tank 10 of the electroplating treatment section 3 is used to clean the dust adhered to the surface of the article to be plated (the article to be plated after removing grease, oxides, and the like in the pretreatment section 2). The upstream tank 10 is composed of a plurality of (two) tanks for storing and storing water.滚筒 When the drum moves from the upstream side to the downstream side and is positioned above each upstream tank 10, it moves downward and is disposed in the upstream tank 10. Then, the drum is rotated in a state of being disposed in the upstream tank 10, whereby the to-be-plated product in the drum is washed with water. The upstream groove 10 can also be constituted by one groove.上游 In addition, the upstream tank 10 may be configured not to wash the plated product with water, but to treat the surface of the plated product with a surfactant such as dilute hydrochloric acid or dilute nitric acid. In addition, the upstream tank 10 may be configured so that the surface of the object to be plated is treated with a surfactant after the object to be plated is washed with water.

電鍍處理部3的電鍍槽11,是對在上游槽10中被洗淨後的被鍍品實施電鍍處理。電鍍槽11是由供蓄積電鍍液之複數個(10個)槽所構成。   當滾筒從上游側往下游側移動而位於各電鍍槽11的上方時,會往下方移動而配置在電鍍槽11內。而且,在配置於電鍍槽11內的狀態下讓滾筒旋轉,藉此對滾筒內的被鍍品實施電鍍處理。The plating tank 11 of the plating processing section 3 performs a plating process on the articles to be plated that have been washed in the upstream tank 10. The plating tank 11 is composed of a plurality of (10) tanks for storing a plating solution.滚筒 When the drum moves from the upstream side to the downstream side and is positioned above each plating tank 11, it moves downward and is disposed in the plating tank 11. Then, the drum is rotated in a state of being disposed in the plating tank 11, whereby the plated product in the drum is subjected to a plating treatment.

電鍍處理部3的回收槽12,是將在電鍍槽11中被實施電鍍處理後之被鍍品上所附著的電鍍液回收。當滾筒從上游側往下游側移動而位於回收槽12的上方時,會往下方移動而配置在回收槽12內。而且,在回收槽12內配置有滾筒的狀態下,讓滾筒的軸心成為以既定角度(例如40度)傾斜的狀態,將在被鍍品上所附著的電鍍液回收。   被回收的電鍍液,是透過回流管20返回電鍍槽11。回流管20是連結於回收槽12和電鍍槽11。   回收槽12也能構成為,利用吸引裝置進行吸引、讓滾筒旋轉等,藉此將在被鍍品上所附著的電鍍液回收。The recovery tank 12 of the plating processing unit 3 collects the plating solution adhered to the to-be-plated product after the plating processing is performed in the plating tank 11. When the drum moves from the upstream side to the downstream side and is located above the recovery tank 12, it moves downward and is disposed in the recovery tank 12. Then, in a state where a roller is disposed in the recovery tank 12, the axis of the roller is inclined at a predetermined angle (for example, 40 degrees), and the plating solution adhered to the object to be plated is recovered. The recovered plating solution is returned to the plating tank 11 through the return pipe 20. The return pipe 20 is connected to the recovery tank 12 and the plating tank 11. The krypton recovery tank 12 can also be configured to collect a plating solution adhered to a to-be-plated product by suction using a suction device, rotating a drum, or the like.

電鍍處理部3的水洗槽13,是將未被回收槽12回收而在被鍍品上所附著的電鍍液洗淨。水洗槽13是由供蓄水之複數個(例如三個)槽(逆流多段水洗)所構成。   當滾筒從上游側往下游側移動而位於各水洗槽13的上方時,會往下方移動而配置在水洗槽13內。而且,在配置於水洗槽13內的狀態下讓滾筒旋轉,藉此將滾筒內的被鍍品用水洗淨。   水洗槽13當中之最下游側的槽,為了在水洗槽13之下游側將被鍍品的洗淨效果提高、將乾燥時間縮短,也能構成為供蓄積熱水(熱水洗槽)。The water washing tank 13 of the plating treatment section 3 cleans the plating solution attached to the object to be plated without being recovered by the recovery tank 12. The water washing tank 13 is composed of a plurality of (for example, three) tanks (counter-current multi-stage water washing) for storing and storing water. (2) When the drum moves from the upstream side to the downstream side and is positioned above each of the water washing tanks 13, the drum moves downward and is arranged in the water washing tanks 13. Then, the drum is rotated in a state of being disposed in the water washing tank 13, thereby washing the to-be-plated product in the drum with water. The most downstream side of the water washing tank 13 can be configured to store hot water (hot water washing tank) in order to improve the cleaning effect of the plated product on the downstream side of the water washing tank 13 and shorten the drying time.

後處理部4,是將在電鍍處理部3中結束電鍍處理後之被鍍品從滾筒取出,進行為了讓該被鍍品之鋅金屬表面的耐蝕性提高的處理(例如,鉻酸處理)、或為了在隨後進行的塗裝工序中讓該被鍍品的塗膜密合性提高的處理(例如,磷酸處理)等。The post-processing unit 4 is a process (for example, chromic acid treatment) for removing the object to be plated after the electroplating process in the electroplating process part 3 from the drum, in order to improve the corrosion resistance of the zinc metal surface of the object to be plated, Or a process (for example, a phosphoric acid process) etc. for improving the adhesiveness of the coating film of this to-be-plated object in the coating process performed later.

中間坑6是形成於用於配置電鍍鋅裝置1之地板下。   中間坑6,是將在電鍍處理部3之上游槽10及水洗槽13中蓄積的水(在被鍍品的洗淨中所使用的水)回收並暫時貯留。此外,中間坑6,是將在後處理部4中實施鉻酸處理後用於洗淨之水洗槽中所蓄積的水、或實施磷酸處理後用於洗淨之水洗槽中所蓄積的水(在被鍍品的洗淨中所使用的水)回收並暫時貯留。   在電鍍處理部3之上游槽10以及水洗槽13中所蓄積的水,是透過回收管21而由中間坑6回收。回收管21是連結於電鍍處理部3之上游槽10及水洗槽13和中間坑6。   在後處理部4中實施鉻酸處理後用於洗淨之水洗槽中所蓄積的水、或實施磷酸處理後用於洗淨之水洗槽中所蓄積的水,是透過回收管22而由中間坑6回收。回收管22是連結於:在後處理部4中實施鉻酸處理後用於洗淨之水洗槽、或實施磷酸處理後用於洗淨之水洗槽、和中間坑6。The intermediate pit 6 is formed under the floor where the electrogalvanizing apparatus 1 is arranged. The intermediate pit 6 collects and temporarily stores water (water used for washing the plated product) stored in the upstream tank 10 and the water washing tank 13 of the plating treatment section 3. In addition, the middle pit 6 is the water stored in the water washing tank for washing after the chromic acid treatment is performed in the post-processing section 4, or the water stored in the water washing tank for washing after the phosphoric acid treatment ( Water used for cleaning the plated product is recovered and temporarily stored. The water accumulated in the upstream tank 10 and the water washing tank 13 of the plating treatment section 3 is recovered by the intermediate pit 6 through the recovery pipe 21. The recovery pipe 21 is connected to the upstream tank 10, the water washing tank 13, and the intermediate pit 6 of the plating treatment section 3. The water stored in the water washing tank for the washing after the chromic acid treatment is performed in the post-treatment section 4 or the water stored in the water washing tank for the washing after the phosphoric acid treatment is performed is passed through the recovery pipe 22 to the middle. Pit 6 is recycled. The recovery pipe 22 is connected to a water washing tank for washing after the chromic acid treatment is performed in the post-treatment section 4, or a water washing tank for washing after the phosphoric acid treatment is performed, and the intermediate pit 6.

水處理部5是進行在中間坑6所蓄積的水(在被鍍品的洗淨中所使用的水)之處理。水處理部5係具備:回收水箱(water tank)30、蒸餾裝置31(減壓脫水處理裝置)以及再生水箱32。The water treatment unit 5 performs the treatment of the water (water used for washing the plated product) stored in the intermediate pit 6. The water treatment unit 5 includes a recovery water tank 30, a distillation device 31 (a reduced-pressure dehydration treatment device), and a regeneration water tank 32.

在中間坑6所蓄積的水,是透過回收管23而由水處理部5之回收水箱30回收。回收管23是連結於中間坑6和水處理部5。   水處理部5,是將回收水箱30內的水(在被鍍品的洗淨中所使用的水)在蒸餾裝置31中進行真空減壓而以沸點降低的狀態進行蒸餾,讓其分離成水(再生水)、脫水後之固態廢棄物。在水處理部5,在蒸餾裝置31中被分離後的水是貯留於再生水箱32,脫水後的固態廢棄物則被廢棄。The water accumulated in the intermediate pit 6 is recovered by the recovery water tank 30 of the water treatment unit 5 through the recovery pipe 23. The recovery pipe 23 is connected to the intermediate pit 6 and the water treatment unit 5. The water treatment unit 5 is configured to distill the water in the recovered water tank 30 (water used for washing the plated product) in the distillation device 31 under reduced pressure in a vacuum to distill the boiling point and separate it into water. (Recycled water), solid waste after dehydration. In the water treatment unit 5, the water separated in the distillation device 31 is stored in the reclaimed water tank 32, and the dehydrated solid waste is discarded.

在水處理部5之再生水箱32中所蓄積的水,是透過供給管24供給到電鍍處理部3之上游槽10或水洗槽13。供給管24是連結於電鍍處理部3之上游槽10或水洗槽13、和水處理部5之再生水箱32。   此外,在水處理部5之再生水箱32中所蓄積的水,作為用於洗淨被鍍品的水,是透過供給管24供給到後處理部4之鉻酸處理後用於洗淨之水洗槽、或磷酸處理後用於洗淨之水洗槽。供給管24是連結於:後處理部4之鉻酸處理後用於洗淨之水洗槽、或磷酸處理後用於洗淨之水洗槽。   在供給管24配備有過濾器33(例如活性碳過濾器),在中間坑6蓄積的水,是藉由過濾器33將雜質過濾而進行流通。The water stored in the reclaimed water tank 32 of the water treatment section 5 is supplied to the upstream tank 10 or the water washing tank 13 of the plating treatment section 3 through the supply pipe 24. The supply pipe 24 is connected to the upstream tank 10 or the water washing tank 13 of the plating treatment section 3 and the regeneration water tank 32 of the water treatment section 5. In addition, the water stored in the reclaimed water tank 32 of the water treatment unit 5 is used for washing the to-be-plated product, and is washed with water after the chromic acid treatment is supplied to the post-treatment unit 4 through the supply pipe 24. Tank or water washing tank for washing after phosphoric acid treatment. The supply pipe 24 is connected to a water washing tank for washing after the chromic acid treatment in the post-processing section 4 or a water washing tank for washing after the phosphoric acid treatment.供给 A filter 33 (for example, an activated carbon filter) is provided in the supply pipe 24, and water accumulated in the middle pit 6 is filtered by the filter 33 to circulate impurities.

接下來說明,電鍍鋅裝置1中之在被鍍品的表面形成鍍鋅被膜的處理之一系列的動作。Next, a series of operations of the process of forming a galvanized film on the surface of a to-be-plated article in the galvanizing apparatus 1 is demonstrated.

如圖2所示般,在電鍍鋅裝置1,在前處理部2之脫脂處理部7中,進行將被鍍品的表面之油脂去除的處理(脫脂處理)(步驟S1)。   這時,在前處理部2之脫脂處理部7中,使用既定的溶劑進行被鍍品的表面之脫脂處理。例如,在前處理部2之脫脂處理部7,使用有機溶劑將被鍍品的表面之油脂溶解,藉此進行脫脂處理。   在前處理部2之脫脂處理部7中進行將被鍍品的表面之油脂去除的工序後,移至步驟S2。As shown in FIG. 2, in the galvanizing apparatus 1, the degreasing treatment section 7 of the pretreatment section 2 performs a process (degreasing treatment) for removing grease on the surface of the object to be plated (step S1). At this time, in the degreasing treatment section 7 of the pretreatment section 2, a predetermined solvent is used to perform a degreasing treatment on the surface of the object to be plated. For example, in the degreasing treatment section 7 of the pretreatment section 2, an organic solvent is used to dissolve the grease on the surface of the object to be plated, thereby performing a degreasing treatment.进行 After the step of removing grease from the surface of the object to be plated is performed in the degreasing treatment section 7 of the pretreatment section 2, the process proceeds to step S2.

接下來,在電鍍鋅裝置1,在前處理部2之底層調整部8中,進行被實施脫脂處理後之被鍍品的表面之底層調整(步驟S2)。   這時,在底層調整部8中,噴射研磨劑來將被鍍品的表面之氧化物、鏽等去除,藉此進行被鍍品的表面之底層調整。   在前處理部2之底層調整部8中進行將被鍍品的表面實施底層調整的工序後,移至步驟S3。Next, in the electro-galvanizing apparatus 1, the bottom layer adjustment section 8 of the pre-processing section 2 performs the bottom layer adjustment of the surface of the object to be plated after the degreasing treatment is performed (step S2). At this time, in the underlayer adjusting portion 8, abrasives are sprayed to remove oxides, rust, and the like on the surface of the object to be plated, thereby adjusting the underlayer of the surface of the object to be plated. (1) After performing the step of adjusting the surface of the object to be plated in the bottom layer adjusting section 8 of the pre-processing section 2, the process proceeds to step S3.

接下來,在電鍍鋅裝置1,在電鍍處理部3中,對被鍍品的表面使用電鍍液進行電鍍處理(步驟S3)。   在電鍍處理部3中,進行對被鍍品的表面使用電鍍液實施電鍍處理的工序後,移至步驟S4。Next, in the galvanizing apparatus 1, in the plating processing part 3, the surface of the to-be-plated object is electroplated using the electroplating solution (step S3). (2) In the electroplating treatment unit 3, after performing the step of performing electroplating treatment on the surface of the object to be plated using a plating solution, the process proceeds to step S4.

接下來,在電鍍鋅裝置1,在後處理部4中,進行為了讓被鍍品之鋅金屬表面的耐蝕性提高的處理、或為了在隨後進行之塗裝工序中讓被鍍品的塗膜密合性提高之處理等(步驟S4)。   在電鍍鋅裝置1,在後處理部4中,進行為了讓被鍍品之鋅金屬表面的耐蝕性提高的處理、或為了在隨後進行之塗裝工序中讓被鍍品的塗膜密合性提高之處理等的工序後,將其動作結束。   如此般,在電鍍鋅裝置1進行在被鍍品的表面形成鍍鋅被膜之處理。Next, in the galvanizing apparatus 1, in the post-processing section 4, a treatment is performed to improve the corrosion resistance of the zinc metal surface of the object to be plated, or a coating film is provided to the object to be plated in a subsequent coating process. Processing for improving the adhesion (step S4). In the electro-galvanizing apparatus 1, in the post-processing section 4, a treatment is performed to improve the corrosion resistance of the zinc metal surface of the object to be plated, or to make the coating film adherence of the object to be plated in a subsequent coating process. After the steps such as the raising process, the operation is terminated. In this way, the galvanizing apparatus 1 performs a process of forming a galvanized film on the surface of the object to be plated.

如以上般,在電鍍鋅裝置1(電鍍鋅方法)之前處理部2(前處理部2之脫脂處理部7),使用既定溶劑進行被鍍品的表面之脫脂處理,在前處理部2中,鹼性脫脂後之水洗及電解脫脂後之水洗都不需要,而以無排水的方式進行將被鍍品的表面之油脂去除的處理。因此,在電鍍鋅裝置1(電鍍鋅方法),當進行在被鍍品的表面形成鍍鋅被膜之處理時,能夠將在被鍍品的水洗中所使用的水之排水量大幅減少(從每一小時數百公升減少到數十公升)。   因此,在電鍍鋅裝置1(電鍍鋅方法),在鹼性脫脂後之水洗中所使用的水之排水設備、以及在電解脫脂後之水洗中所使用的水之排水設備等都不需要,排水設備可採用便宜的構造。As described above, before the electroplating apparatus 1 (galvanizing method), the pretreatment section 2 (the degreasing treatment section 7 of the pretreatment section 2) uses a predetermined solvent to perform degreasing treatment on the surface of the object to be plated. In the pretreatment section 2, Water washing after alkaline degreasing and water washing after electrolytic degreasing are not required, and the surface is treated without oil and grease to remove the grease. Therefore, in the galvanizing apparatus 1 (galvanizing method), when the process of forming a galvanized film on the surface of the object to be plated is performed, the drainage amount of water used in the washing of the object to be plated can be greatly reduced (from each Hundreds of liters per hour were reduced to tens of liters). Therefore, in the electrogalvanizing apparatus 1 (electrolytic galvanization method), water drainage equipment used in the washing after alkaline degreasing, and water drainage equipment used in the washing after electrolytic degreasing are not required. The device can adopt an inexpensive construction.

如以上般,在電鍍鋅裝置1(電鍍鋅方法)之前處理部2(前處理部2之脫脂處理部7),使用有機溶劑將被鍍品的表面之油脂溶解來進行脫脂處理,在前處理部2中,鹼性脫脂後的水洗及電解脫脂後的水洗都不需要,而以無排水的方式進行將被鍍品的表面之油脂去除的處理。   因此,在電鍍鋅裝置1(電鍍鋅方法),當進行在被鍍品的表面形成鍍鋅被膜的處理時,能夠將在被鍍品的水洗中所使用的水之排水量大幅減少(從每一小時數百公升減少到數十公升)。   因此,在電鍍鋅裝置1(電鍍鋅方法),在鹼性脫脂後之水洗中所使用的水之排水設備、以及在電解脫脂後的水洗中所使用的水之排水設備等都不需要,排水設備可採用便宜的構造。As described above, before the galvanizing apparatus 1 (galvanizing method), the pre-treatment section 2 (the degreasing treatment section 7 of the pre-treatment section 2) uses an organic solvent to dissolve the grease on the surface of the plated product to perform a degreasing treatment. In Part 2, water washing after alkaline degreasing and water washing after electrolytic degreasing are not required, and the treatment for removing grease from the surface of the plated product is performed without drainage. Therefore, in the galvanizing apparatus 1 (galvanizing method), when the process of forming a galvanized film on the surface of the object to be plated is performed, the drainage amount of water used for washing the object to be plated can be greatly reduced (from each Hundreds of liters per hour were reduced to tens of liters). Therefore, in the electro-galvanizing device 1 (electro-galvanizing method), water drainage equipment used in water washing after alkaline degreasing, and water drainage equipment used in water washing after electrolytic degreasing are not required. The device can adopt an inexpensive construction.

如以上般,在電鍍鋅裝置1(電鍍鋅方法)之前處理部2(前處理部2之底層調整部8),對被實施脫脂處理後之被鍍品的表面噴射研磨劑來進行被鍍品的表面之底層調整,在前處理部2中,利用鹽酸等進行酸洗淨後的水洗並不需要,而以無排水的方式進行將被鍍品的表面之氧化物去除的處理。   因此,在電鍍鋅裝置1(電鍍鋅方法),當進行在被鍍品的表面形成鍍鋅被膜的處理時,能夠將在被鍍品的水洗中所使用之水的排水量大幅減少(從每一小時數百公升減少到數十公升)。   因此,在電鍍鋅裝置1(電鍍鋅方法),利用鹽酸等進行酸洗淨後之水洗中所使用的水之排水設備並不需要,排水設備可採用便宜的構造。As described above, before the galvanizing apparatus 1 (galvanizing method), the pre-treatment section 2 (the bottom layer adjustment section 8 of the pre-treatment section 2) sprays abrasives on the surface of the plated product after the degreasing treatment to perform the plated product. In the pre-treatment section 2, the pre-processing section 2 does not require water washing after pickling with hydrochloric acid or the like, but performs a treatment for removing oxides on the surface of the plated product in a non-draining manner. Therefore, in the galvanizing apparatus 1 (galvanizing method), when the process of forming a galvanized film on the surface of the object to be plated is performed, the drainage amount of water used for washing the object to be plated can be greatly reduced (from each Hundreds of liters per hour were reduced to tens of liters). Therefore, in the galvanizing apparatus 1 (galvanizing method), the drainage equipment for water used in the water washing after pickling with hydrochloric acid or the like is not necessary, and the drainage equipment can have an inexpensive structure.

如以上般,在電鍍鋅裝置1(電鍍鋅方法)之前處理部2(前處理部2之脫脂處理部7以及底層調整部8),使用有機溶劑將被鍍品的表面之油脂溶解來進行脫脂處理、對被實施脫脂處理後之被鍍品的表面噴射研磨劑來進行被鍍品的表面之底層調整,在前處理部2中,鹼性脫脂後的水洗、利用鹽酸等進行酸洗淨後的水洗、以及電解脫脂後的水洗都不需要,而以無排水的方式進行將被鍍品的表面之油脂及氧化物等去除的處理。   因此,在電鍍鋅裝置1(電鍍鋅方法),當進行在被鍍品的表面形成鍍鋅被膜的處理時,能夠將在被鍍品的水洗中所使用之水的排水量大幅減少(從每一小時數百公升減少到數十公升)。   因此,在電鍍鋅裝置1(電鍍鋅方法),在鹼性脫脂後的水洗中所使用的水之排水設備、在電解脫脂後的水洗中所使用的水之排水設備、以及在利用鹽酸等進行酸洗淨後之水洗中所使用的水之排水設備等都不需要,排水設備可採用便宜的構造。   因此,在電鍍鋅裝置1(電鍍鋅方法),除了可將全體的排水量大幅減少,含有鹼性脫脂劑、乳化後的油脂分、以及酸洗淨所使用的鹽酸等和被其溶解後的金屬之水的處理是不需要的,如此能使水處理部5小型化。As described above, before the electroplating apparatus 1 (galvanizing method), the pretreatment section 2 (the degreasing treatment section 7 and the bottom layer adjustment section 8 of the pretreatment section 2) dissolves the grease on the surface of the plated product with an organic solvent to perform degreasing. Treatment, spraying abrasives on the surface of the plated product after degreasing treatment to adjust the bottom layer of the surface of the plated product. In the pretreatment section 2, water washing after alkaline degreasing, acid washing with hydrochloric acid, etc. Water washing and electrolytic washing after degreasing are not required, and the surface of the product to be plated is treated with grease and oxides without drainage. Therefore, in the galvanizing apparatus 1 (galvanizing method), when the process of forming a galvanized film on the surface of the object to be plated is performed, the drainage amount of water used for washing the object to be plated can be greatly reduced (from each Hundreds of liters per hour were reduced to tens of liters). Therefore, in the electro-galvanizing apparatus 1 (electro-galvanizing method), water drainage equipment used in water washing after alkaline degreasing, water drainage equipment used in water washing after electrolytic degreasing, and hydrochloric acid are used. The water drainage equipment used in the water washing after the pickling is not required, and the drainage equipment can adopt an inexpensive structure. Therefore, in the electrogalvanizing apparatus 1 (electrogalvanization method), in addition to greatly reducing the overall drainage volume, it contains alkaline degreasing agents, emulsified oils and fats, hydrochloric acid used for pickling, and metals dissolved therein. The treatment of water is unnecessary, so that the water treatment unit 5 can be miniaturized.

如以上般,在電鍍鋅裝置1(電鍍鋅方法)之前處理部2(前處理部之底層調整部8),是對被實施脫脂處理後之被鍍品的表面噴射研磨劑來進行被鍍品的表面之底層調整,而不是進行酸洗淨,因此電鍍處理部3之電鍍槽11(電鍍槽11或電鍍槽11內的電鍍液)可成為未被鐵離子等污染的狀態。亦即,在電鍍鋅裝置1(電鍍鋅方法),因為在前處理部2(前處理部之底層調整部8)中並未進行酸洗淨,不需投入PH調整劑(氨、過氧化氫等)來從電鍍槽11的電鍍液將鐵離子除去。   此外,在電鍍鋅裝置1(電鍍鋅方法),因為在前處理部2(前處理部之底層調整部8)中未進行酸洗淨,可抑制在作業環境中的臭氣發生而使作業環境提高,此外,能夠防止設備、建築物等被酸腐蝕。As described above, before the galvanizing apparatus 1 (galvanizing method), the pre-treatment section 2 (the bottom layer adjustment section 8 of the pre-treatment section) sprays abrasives on the surface of the plated product after the degreasing treatment to perform the plated product. The bottom layer of the surface is adjusted instead of being acid-washed. Therefore, the plating bath 11 (the plating bath 11 or the plating solution in the plating bath 11) of the plating treatment section 3 can be in a state not contaminated by iron ions and the like. That is, in the galvanizing apparatus 1 (galvanizing method), since the pre-treatment section 2 (the bottom-layer adjustment section 8 of the pre-treatment section) is not acid-washed, it is not necessary to input a pH adjuster (ammonia, hydrogen peroxide). Etc.) to remove iron ions from the plating solution of the plating tank 11. In addition, in the galvanizing apparatus 1 (galvanizing method), since the pretreatment section 2 (the bottom layer adjustment section 8 of the pretreatment section) is not pickled, the occurrence of odor in the work environment can be suppressed and the work environment can be suppressed. It can also prevent corrosion of equipment, buildings, etc. by an acid.

如以上般,在電鍍鋅裝置1(電鍍鋅方法)之前處理部2(前處理部之脫脂處理部7),是使用有機溶劑將被鍍品的表面之油脂溶解來進行脫脂處理,因為未進行電解脫脂,可降低被實施電鍍處理後的物品發生氫脆化的風險。As described above, before the galvanizing apparatus 1 (galvanizing method), the pretreatment section 2 (the degreasing treatment section 7 of the pretreatment section) uses an organic solvent to dissolve the grease on the surface of the plated product, because the degreasing treatment is not performed. Electrolytic degreasing can reduce the risk of hydrogen embrittlement of articles after plating.

又如以上般,在電鍍鋅裝置1(電鍍鋅方法)之水處理部5,將在電鍍處理部3中在被鍍品的洗淨中所使用的水蒸餾而分離成水(再生水)和固態廢棄物,並將該分離後的水(再生水)作為用於洗淨被鍍品的水而供給到電鍍處理部3之上游槽10或水洗槽13,因此可將在電鍍處理部3中在被鍍品的洗淨中所使用的水予以再利用,不需將在該被鍍品的洗淨中所使用的水進行處理而實施放流(排水)。   因此,在電鍍鋅裝置1(電鍍鋅方法),為了符合預料會日趨嚴格之在被鍍品的洗淨中所使用的水的排水基準,不需導入高價的排水處理設備。In the same manner as above, in the water treatment section 5 of the galvanizing apparatus 1 (galvanization method), the water used for washing the plated product in the electroplating treatment section 3 is distilled and separated into water (reclaimed water) and solid. Waste, and the separated water (recycled water) is supplied to the upstream tank 10 or the water washing tank 13 of the plating treatment section 3 as water for washing the plated product. Therefore, the water in the plating treatment section 3 can be cleaned. The water used for washing the plated product is reused, and it is not necessary to treat the water used for washing the plated product to drain (drain). Therefore, in the electrogalvanizing apparatus 1 (galvanizing method), it is not necessary to introduce expensive drainage treatment equipment in order to meet the drainage standards for water used for cleaning of plated products, which are expected to become stricter.

又如以上般,在電鍍鋅裝置1(電鍍鋅方法)之水處理部5,將在後處理部4中在被鍍品的洗淨中所使用的水蒸餾,讓其分離成水(再生水)和固態廢棄物,並將該分離後的(再生水)作為用於洗淨被鍍品的水而供給到後處理部4之鉻酸處理後用於洗淨的水洗槽、或磷酸處理後用於洗淨之水洗槽,將在後處理部4中在被鍍品的洗淨中所使用的水予以再利用,不需將在該被鍍品的洗淨中所使用的水進行處理而實施放流(排水)。   因此,在電鍍鋅裝置1(電鍍鋅方法), 為了符合預料會日趨嚴格之在被鍍品的洗淨中所使用的水的排水基準,不需導入高價的排水處理設備。As described above, in the water treatment section 5 of the galvanizing apparatus 1 (galvanizing method), the water used for washing the plated product in the post-treatment section 4 is distilled and separated into water (reclaimed water). And solid waste, and this separated (recycled water) is supplied to the post-processing section 4 as water for washing the plated product, and is used in a water washing tank for washing after chromic acid treatment or for phosphoric acid treatment. The washing water washing tank reuses the water used in the washing of the plated product in the post-processing unit 4 without draining the water used in the washing of the plated product. (drain). Therefore, in the electrogalvanizing apparatus 1 (galvanizing method), it is not necessary to introduce expensive drainage treatment equipment in order to meet the drainage standards for water used for cleaning of plated products, which are expected to become stricter.

如圖3所示般,電鍍鋅裝置1亦可構成為,具備有:前處理部2、電鍍處理部3、後處理部4及水處理部5,但不具備中間坑6。As shown in FIG. 3, the galvanizing apparatus 1 may be configured to include a pre-treatment section 2, a plating treatment section 3, a post-treatment section 4, and a water treatment section 5, but does not include the intermediate pit 6.

水處理部5,是對應於供蓄積所回收的水之槽(所回收的水之成分),而具備複數個回收水箱30。水處理部5,是對於每個供蓄積所回收的水之槽(所回收的水之成分),設置回收水箱30。水處理部5係具備:用於回收在電鍍處理部3的上游槽10所蓄積的水之回收水箱30a、用於回收在電鍍處理部3的水洗槽13所蓄積的水之回收水箱30b、用於回收在後處理部4的水洗槽所蓄積的水之回收水箱30c。The water treatment unit 5 is provided with a plurality of recovery water tanks 30 corresponding to a tank (a component of the recovered water) for storing the recovered water. The water treatment unit 5 is provided with a recovery water tank 30 for each tank (a component of the recovered water) for storing the recovered water. The water treatment section 5 includes a recovery water tank 30 a for recovering water stored in the upstream tank 10 of the plating treatment section 3, a recovery water tank 30 b for recovering water stored in the washing tank 13 of the plating treatment section 3, and In a recovery water tank 30 c that collects water stored in the water washing tank of the post-processing unit 4.

在電鍍處理部3之上游槽10所蓄積的水,是透過回收管25而由水處理部5之回收水箱30a回收。回收管25是連結於電鍍處理部3之上游槽10和水處理部5之回收水箱30a。   在電鍍處理部3之水洗槽13所蓄積的水,是透過回收管26而由水處理部5之回收水箱30b回收。回收管26是連結於電鍍處理部3之水洗槽13和水處理部5之回收水箱30b。   在後處理部4之鉻酸處理後用於洗淨之水洗槽所蓄積的水、或磷酸處理後用於洗淨之水洗槽所蓄積的水,是透過回收管27而由水處理部之回收水箱30c回收。回收管27是連結於:後處理部4之鉻酸處理後用於洗淨之水洗槽或磷酸處理後用於洗淨之水洗槽、和水處理部5之回收水箱30c。The water accumulated in the upstream tank 10 of the plating treatment section 3 is recovered by the recovery water tank 30 a of the water treatment section 5 through the recovery pipe 25. The recovery pipe 25 is a recovery water tank 30 a connected to the upstream tank 10 of the plating treatment section 3 and the water treatment section 5. (2) The water accumulated in the water washing tank 13 of the plating treatment section 3 is recovered by the recovery water tank 30b of the water treatment section 5 through the recovery pipe 26. The recovery pipe 26 is connected to the water washing tank 13 of the plating treatment section 3 and the recovery water tank 30 b of the water treatment section 5. The water accumulated in the water washing tank used for washing after the chromic acid treatment in the post-treatment section 4 or the water stored in the water washing tank used for washing after the phosphoric acid treatment is recovered by the water treatment section through the recovery pipe 27 The water tank 30c is recovered. The recovery pipe 27 is connected to a water washing tank for washing after the chromic acid treatment in the post-processing unit 4 or a water washing tank for washing after the phosphoric acid treatment, and a recovery water tank 30 c in the water treatment unit 5.

如此般,水處理部5,因為對於每個供蓄積所回收的水之槽(所回收的水之成分),設置有回收水箱30(回收水箱30a,30b,30c),相較於從複數個槽將水回收到一個回收水箱30的處理,可容易且確實地進行將回收水箱30內的水(在被鍍品的洗淨中所使用的水)在蒸餾裝置31中實施真空減壓以沸點降低的狀態蒸餾而分離成水(再生水)和脫水後的固態廢棄物之處理。In this way, the water treatment unit 5 is provided with a recovery water tank 30 (recovery water tanks 30a, 30b, 30c) for each of the tanks (components of the recovered water) for storing the recovered water, as compared with a plurality of water tanks. The process of recovering water to a single recovery water tank 30 can easily and reliably perform the water in the recovery water tank 30 (water used for washing the plated product) in the distillation device 31 under vacuum to reduce the boiling point. Distillation in a reduced state to separate water (recycled water) and dehydrated solid waste.

電鍍鋅裝置1之水處理部5亦可構成為,在電鍍處理部3所使用而回收的水、在後處理部4所使用而回收的水,不是利用共用的蒸餾裝置31、再生水箱32、或過濾器33等進行處理,而是分別個別進行成為再生水的處理。   如圖4所示般,水處理部5係具備:回收水箱30a,30b,30c、蒸餾裝置31a,31c、再生水箱32a,32c、過濾器33a,33c。The water treatment section 5 of the galvanizing device 1 may be configured such that the water recovered and used in the electroplating treatment section 3 and the water recovered and used in the post-treatment section 4 are not used by the common distillation device 31, the regeneration water tank 32, Or the filter 33 or the like performs the treatment, but the treatment to be the recycled water is performed individually. As shown in FIG. 4, the water treatment unit 5 includes: recovery water tanks 30 a, 30 b, and 30 c; distillation apparatuses 31 a and 31 c; regeneration water tanks 32 a and 32 c; and filters 33 a and 33 c.

在電鍍處理部3之上游槽10所蓄積的水,是由水處理部5之回收水箱30a回收;在電鍍處理部3之水洗槽13所蓄積的水,是由水處理部5之回收水箱30b回收;在後處理部4之鉻酸處理後用於洗淨之水洗槽所蓄積的水、或磷酸處理後用於洗淨之水洗槽所蓄積的水,是由水處理部之回收水箱30c。   水處理部5,是將回收水箱30a,30b內的水(在被鍍品的洗淨中所使用的水)在蒸餾裝置31a中分離成水(再生水)和脫水後的固態廢棄物。在水處理部5,在蒸餾裝置31a中分離後的水貯留於再生水箱32a,利用過濾器33a將雜質過濾後供給到:電鍍處理部3的上游槽10或水洗槽13、後處理部4之鉻酸處理後用於洗淨之水洗槽或磷酸處理後用於洗淨之水洗槽。   此外,水處理部5,是將回收水箱30c內的水(在被鍍品的洗淨中所使用的水)在蒸餾裝置31c中分離成水(再生水)和脫水後的固態廢棄物。在水處理部5,在蒸餾裝置31c中分離後的水貯留於再生水箱32c,利用過濾器33c將雜質過濾後供給到:電鍍處理部3的上游槽10或水洗槽13、後處理部4之鉻酸處理後用於洗淨之水洗槽或磷酸處理後用於洗淨之水洗槽。The water accumulated in the upstream tank 10 of the electroplating treatment section 3 is recovered by the recovery water tank 30a of the water treatment section 5; the water accumulated in the water washing tank 13 of the electroplating treatment section 3 is recovered by the recovery water tank 30b of the water treatment section 5 Recovery; The water accumulated in the water washing tank for washing after the chromic acid treatment in the post-processing section 4 or the water accumulated in the water washing tank for washing after the phosphoric acid treatment is collected by the recovery water tank 30c of the water treatment section. The water treatment unit 5 separates water (recycled water) and dehydrated solid waste in the distillation device 31a from the water in the recovered water tanks 30a and 30b (water used for washing the plated product). In the water treatment section 5, the water separated in the distillation device 31a is stored in the reclaimed water tank 32a, and the impurities are filtered by the filter 33a and then supplied to: the upstream tank 10 or the water washing tank 13 of the plating treatment section 3, and the post-treatment section 4 After washing with chromic acid, it is used for washing with water, or after washing with phosphoric acid, it is used for washing with water. In addition, the water treatment unit 5 separates water (recycled water) and dehydrated solid waste in the distillation device 31c in the recovery water tank 30c (water used for washing the plated product). In the water treatment section 5, the water separated in the distillation device 31c is stored in the reclaimed water tank 32c, and the impurities are filtered by the filter 33c and supplied to: the upstream tank 10 or the water washing tank 13 of the plating treatment section 3, and the post-treatment section 4 After washing with chromic acid, it is used for washing with water, or after washing with phosphoric acid, it is used for washing with water.

如此般,水處理部5,將在電鍍處理部3所使用的水、在後處理部4所使用的水,分別在不同的蒸餾裝置31a,31c中進行蒸餾而分離成水(再生水)和脫水後的固態廢棄物,將該蒸餾後的水分別在不同的再生水箱32a,32c中貯留,分別在不同的過濾器33a,33c中將雜質過濾後供給到電鍍處理部3或後處理部4等,相較於將在電鍍處理部3所使用的水、在後處理部4所使用的水用一個蒸餾裝置31蒸餾,並將該蒸餾後的水在一個再生水箱32中貯留且在一個過濾器33中將雜質過濾的情況,能夠容易且確實地進行成為再生水的處理。In this way, the water treatment section 5 separates the water used in the electroplating treatment section 3 and the water used in the post-treatment section 4 in different distillation apparatuses 31a and 31c to separate water (reclaimed water) and dehydration. After the solid waste is removed, the distilled water is stored in different reclaimed water tanks 32a and 32c, and impurities are filtered in different filters 33a and 33c and supplied to the plating processing section 3 or the post-processing section 4, etc. Compared with the water used in the electroplating treatment section 3 and the water used in the post-treatment section 4 are distilled by a distillation device 31, the distilled water is stored in a reclaimed water tank 32 and in a filter In the case where the impurities are filtered in 33, the treatment to be reclaimed water can be easily and reliably performed.

水處理部5也能構成為,將回收水箱30a,30c內的水在共用的蒸餾裝置31(例如蒸餾裝置31a)中分離成水(再生水)和脫水後的固態廢棄物。這時,水處理部5構成為,將回收水箱30b內的水在其他蒸餾裝置31(例如蒸餾裝置31c)中分離成水(再生水)和脫水後的固態廢棄物。   此外,水處理部5亦可構成為,將回收水箱30b,30c內的水在共用的蒸餾裝置31(例如蒸餾裝置31a)中分離成水(再生水)和脫水後的固態廢棄物。這時,水處理部5構成為,將回收水箱30a內的水在其他蒸餾裝置31(例如蒸餾裝置31c)中分離成水(再生水)和脫水後的固態廢棄物,或讓回收水箱30a內的水不透過蒸餾裝置31(蒸餾裝置31c)而直接流到過濾器33(過濾器33c)。   依據這樣的構成,相較於將在電鍍處理部3之上游槽10所使用的水、在電鍍處理部3之水洗槽13所使用的水、以及在後處理部4之水洗槽所使用的水,用一個蒸餾裝置31蒸餾後,將該蒸餾後的水在一個再生水箱32中貯留並在一個過濾器33中將雜質過濾的情況,可容易且確實地進行成為再生水的處理。The water treatment unit 5 may be configured to separate the water in the recovered water tanks 30a, 30c into water (recycled water) and dehydrated solid waste in a common distillation apparatus 31 (for example, the distillation apparatus 31a). At this time, the water treatment unit 5 is configured to separate the water in the recovered water tank 30b into water (recycled water) and dehydrated solid waste in another distillation apparatus 31 (for example, the distillation apparatus 31c). In addition, the water treatment unit 5 may be configured to separate the water in the recovered water tanks 30b and 30c into water (recycled water) and dehydrated solid waste in a common distillation device 31 (for example, the distillation device 31a). At this time, the water treatment unit 5 is configured to separate the water in the recovered water tank 30a into water (recycled water) and dehydrated solid waste in another distillation apparatus 31 (for example, the distillation apparatus 31c), or let the water in the recovered water tank 30a It does not pass through the distillation apparatus 31 (distillation apparatus 31c), but flows directly to the filter 33 (filter 33c). According to this configuration, compared with the water used in the upstream tank 10 of the plating processing section 3, the water used in the water washing tank 13 of the plating processing section 3, and the water used in the water washing tank of the post-processing section 4 In a case where the distilled water is distilled by a distillation device 31, the distilled water is stored in a reclaimed water tank 32 and the impurities are filtered in a filter 33, and the treatment to become reclaimed water can be easily and surely performed.

1‧‧‧電鍍鋅裝置1‧‧‧ Electro-galvanizing device

2‧‧‧前處理部2‧‧‧Pre-treatment Department

3‧‧‧電鍍處理部3‧‧‧Plating treatment department

4‧‧‧後處理部4‧‧‧ Post-processing Department

5‧‧‧水處理部5‧‧‧Water Treatment Department

6‧‧‧中間坑6‧‧‧ middle pit

7‧‧‧脫脂處理部7‧‧‧Degreasing treatment department

8‧‧‧底層調整部8‧‧‧Bottom adjustment department

10‧‧‧上游槽10‧‧‧ upstream trough

11‧‧‧電鍍槽11‧‧‧plating tank

12‧‧‧回收槽12‧‧‧ Recovery Tank

13‧‧‧水洗槽13‧‧‧washing tank

20‧‧‧回流管20‧‧‧ return tube

21、22、23‧‧‧回收管21, 22, 23‧‧‧ Recovery tube

24‧‧‧供給管24‧‧‧Supply tube

30‧‧‧回收水箱30‧‧‧Recycling water tank

31‧‧‧蒸餾裝置31‧‧‧distillation unit

32‧‧‧再生水箱32‧‧‧Recycled water tank

33‧‧‧過濾器33‧‧‧ Filter

圖1係顯示本發明的實施形態之電鍍鋅裝置的方塊圖。   圖2係顯示本發明的實施形態之電鍍鋅裝置的動作之流程圖。   圖3係顯示本發明的實施形態之電鍍鋅裝置的方塊圖。   圖4係顯示本發明的實施形態之電鍍鋅裝置的方塊圖。FIG. 1 is a block diagram showing an electro-galvanizing apparatus according to an embodiment of the present invention. Fig. 2 is a flowchart showing the operation of the galvanizing apparatus according to the embodiment of the present invention. FIG. 3 is a block diagram showing an electro-galvanizing apparatus according to an embodiment of the present invention. FIG. 4 is a block diagram showing an electro-galvanizing apparatus according to an embodiment of the present invention.

Claims (6)

一種電鍍鋅裝置,係進行在被鍍品的表面形成鍍鋅被膜的處理之電鍍鋅裝置,其具備有:   進行前述被鍍品的表面之脫脂處理和底層調整之前處理部、以及   對被實施前述脫脂處理及前述底層調整後之被鍍品的表面使用電鍍液進行電鍍處理之電鍍處理部,   前述前處理部,是藉由對前述被鍍品的表面噴射研磨劑,來進行前述被鍍品的表面之底層調整。An electro-galvanizing device is an electro-galvanizing device that performs a process of forming a galvanized coating on a surface of a to-be-plated product, and includes: (1) a degreasing treatment for the surface of the to-be-plated product and a pre-treatment layer for adjusting the bottom layer; and The degreasing treatment and the surface of the to-be-plated product adjusted by the above-mentioned bottom layer are electroplated with an electroplating solution, and the pre-treatment part is made by spraying an abrasive on the surface of the to-be-plated product. Surface bottom adjustment. 如請求項1所述之電鍍鋅裝置,其中,   前述前處理部,是使用既定的溶劑來進行前述被鍍品的表面之脫脂處理。The electro-galvanizing apparatus according to claim 1, wherein: 前 the pre-treatment section performs a degreasing treatment on the surface of the object to be plated using a predetermined solvent. 如請求項1或請求項2所述之電鍍鋅裝置,其中,   前述前處理部,是藉由使用有機溶劑將前述被鍍品的表面之油脂溶解來進行脫脂處理。The electrogalvanizing apparatus according to claim 1 or claim 2, wherein: 前 the pre-treatment section performs degreasing treatment by dissolving grease on the surface of the plated product with an organic solvent. 如請求項1或請求項2所述之電鍍鋅裝置,   其具備水處理部,   該水處理部,是讓在前述電鍍處理部在被鍍品的洗淨中所使用的水分離成水和廢棄物,將該分離後的水作為用於洗淨前述被鍍品的水而供給到前述電鍍處理部。The electrogalvanizing device according to claim 1 or claim 2, 具备 it has a water treatment section, the water treatment section separates the water used in the electroplating treatment section for washing the plated product into water and discards it The separated water is supplied to the plating treatment section as water for washing the object to be plated. 一種電鍍鋅方法,係進行在被鍍品的表面形成鍍鋅被膜的處理之電鍍鋅方法,   其具備:   進行前述被鍍品的表面之脫脂處理的工序、   進行前述被鍍品的表面之底層調整的工序、以及   對被實施前述脫脂處理及前述底層調整後之被鍍品的表面使用電鍍液進行電鍍處理的工序,   進行前述被鍍品的表面之底層調整的工序,是藉由對被實施前述脫脂處理後之被鍍品的表面噴射研磨劑,來進行前述被鍍品的表面之底層調整。An electro-galvanizing method is an electro-galvanizing method for forming a galvanized coating on the surface of a to-be-plated product, which comprises: a step of performing a degreasing treatment on the surface of the to-be-plated product, and 调整 performing a bottom layer adjustment of the surface of the to-be-plated product And the step of performing an electroplating treatment on the surface of the object to be plated after the aforementioned degreasing treatment and the aforementioned underlayer adjustment, and the step of performing the underlayer adjustment of the surface of the object to be plated An abrasive is sprayed on the surface of the object to be plated after the degreasing treatment to adjust the bottom layer of the surface of the object to be plated. 如請求項5所述之電鍍鋅方法,其中,   進行前述被鍍品的表面之脫脂處理的工序,是使用既定的溶劑來進行前述被鍍品的表面之脫脂處理。The galvanizing method according to claim 5, wherein the step of performing a degreasing treatment on the surface of the object to be plated uses a predetermined solvent to perform a degreasing treatment on the surface of the object to be plated.
TW107116234A 2017-05-26 2018-05-14 Electro-galvanizing device and electro-galvanizing method TWI750374B (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2017-104959 2017-05-26
JP2017104959A JP7075573B2 (en) 2017-05-26 2017-05-26 Electro-galvanizing equipment and electro-galvanizing method

Publications (2)

Publication Number Publication Date
TW201900935A true TW201900935A (en) 2019-01-01
TWI750374B TWI750374B (en) 2021-12-21

Family

ID=64449328

Family Applications (1)

Application Number Title Priority Date Filing Date
TW107116234A TWI750374B (en) 2017-05-26 2018-05-14 Electro-galvanizing device and electro-galvanizing method

Country Status (3)

Country Link
JP (1) JP7075573B2 (en)
CN (1) CN108930052B (en)
TW (1) TWI750374B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111979551B (en) * 2020-07-09 2023-04-07 江苏兴达钢帘线股份有限公司 Cleaning method for replacing phosphorization of thermal diffusion plating line
CN112962127A (en) * 2021-01-29 2021-06-15 无锡鹰贝电化学工程有限公司 Electro-galvanizing process for high-strength steel common rail joint
CN114214676B (en) * 2021-12-31 2023-10-13 成都高鑫机械制造有限公司 Galvanization method for metal workpiece

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63219597A (en) * 1987-03-09 1988-09-13 Sumitomo Electric Ind Ltd Surface treatment of metal
JPH04362193A (en) * 1991-06-06 1992-12-15 Kawasaki Steel Corp Production of cr-containing steel sheet excellent in adhesion of electroplating
JP3557782B2 (en) * 1995-06-14 2004-08-25 株式会社神戸製鋼所 Manufacturing method of electrogalvanized steel sheet with excellent appearance
JP3967479B2 (en) 1998-12-02 2007-08-29 株式会社荏原製作所 Plating equipment
JP4362193B2 (en) 2000-02-24 2009-11-11 Necソフト株式会社 Menu system, menu processing method, and recording medium on which menu processing program is recorded
JP2002363795A (en) 2001-06-04 2002-12-18 Matsushita Electric Ind Co Ltd Barrel plating apparatus
JP4485291B2 (en) * 2004-08-23 2010-06-16 サンエイ工業株式会社 Excavator manufacturing method for agricultural machinery and excavator using the same
JP5654536B2 (en) * 2012-09-10 2015-01-14 ヤマハ発動機株式会社 Iron plating equipment
CN104032342B (en) * 2014-06-11 2016-09-14 安徽大地熊新材料股份有限公司 A kind of method improving Sintered NdFeB magnet and electrodeposited coating adhesion
CN105951134A (en) * 2016-06-12 2016-09-21 南通创源电化学科技有限公司 Acid zinc plating technology for automobile braking system
CN105951141A (en) * 2016-07-04 2016-09-21 江苏大学 Three-dimensional surface shot peening jet electrodeposition manufacturing method and device

Also Published As

Publication number Publication date
JP2018199848A (en) 2018-12-20
JP7075573B2 (en) 2022-05-26
CN108930052A (en) 2018-12-04
TWI750374B (en) 2021-12-21
CN108930052B (en) 2023-02-28

Similar Documents

Publication Publication Date Title
TW201900935A (en) Electrogalvanizing device and electroplating method
JP5873606B1 (en) Wire rod cleaning method and apparatus
JP2007031791A (en) Cleaning method for pickled steel strip in continuous pickling treatment line and cleaning apparatus
JP4830513B2 (en) Method and apparatus for cleaning hot dip galvanized steel sheet
JP2011021240A (en) Method for removing scale on steel strip and equipment to be used for execution thereof
RU2691688C2 (en) Method and system for processing strip of carbon steel, primarily for etching
JP6135575B2 (en) Cold-rolled steel sheet cooling method, cooling equipment, and cold-rolled steel sheet manufacturing method
JP2009185371A (en) Apparatus and method for pretreatment of metal product treatment
JP7441023B2 (en) Method and apparatus for processing objects to be processed
JP4751419B2 (en) Electrodeposition water washing system
CN109877092B (en) Surface cleaning system and surface treatment method for metal strip after sand blasting cleaning
JP2786388B2 (en) Manufacturing method and manufacturing equipment for stainless abrasive products
JP6779245B2 (en) Electrodeposition coating equipment
JP4952265B2 (en) Steel strip electroplating equipment and electroplating method
JP2010222602A (en) Pickling method and pickling equipment of metal material
JP7207357B2 (en) Method for pickling metal plate and method for manufacturing metal plate
JP5862269B2 (en) Equipment for preventing metal adhesion to conductor rolls and for preventing metal adhesion on a continuous electroplating line
CN111041460A (en) Chemical plating production process of super-long workpiece
RU2002114220A (en) METHOD FOR DIRECTLESS GALVANOCHEMICAL PROCESSING AND CLEANING OF SURFACE OF PARTS, IN PARTICULAR, ON SUSPENSION
JP2008024982A (en) Plating apparatus
JPH08174042A (en) Cleaning method of metallic strip after cold rolling and device therefor
JP2001131789A (en) Process and equipment for pretreating electroplating steel sheet
JP4862424B2 (en) Wastewater treatment method for stainless steel pickling line
CN105154895A (en) Gear acid pickling process
JPS632436Y2 (en)