JP2021085068A - Method of suppressing increase of zinc concentration of plating solution and production method of zinc-based plated member - Google Patents

Method of suppressing increase of zinc concentration of plating solution and production method of zinc-based plated member Download PDF

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JP2021085068A
JP2021085068A JP2019214897A JP2019214897A JP2021085068A JP 2021085068 A JP2021085068 A JP 2021085068A JP 2019214897 A JP2019214897 A JP 2019214897A JP 2019214897 A JP2019214897 A JP 2019214897A JP 2021085068 A JP2021085068 A JP 2021085068A
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zinc
diaphragm
plating
exchange membrane
tank
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JP6750186B1 (en
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寿裕 杉浦
Hisahiro Sugiura
寿裕 杉浦
泰紀 青木
Yasunori Aoki
泰紀 青木
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Yuken Industry Co Ltd
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Priority to EP20886179.9A priority patent/EP3868924A4/en
Priority to US17/297,470 priority patent/US20220298668A1/en
Priority to MX2021007195A priority patent/MX2021007195A/en
Priority to CN202080006376.7A priority patent/CN113195798A/en
Priority to PCT/JP2020/031629 priority patent/WO2021106291A1/en
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    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D17/00—Constructional parts, or assemblies thereof, of cells for electrolytic coating
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D21/00—Processes for servicing or operating cells for electrolytic coating
    • C25D21/12—Process control or regulation
    • C25D21/14—Controlled addition of electrolyte components
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D17/00—Constructional parts, or assemblies thereof, of cells for electrolytic coating
    • C25D17/002—Cell separation, e.g. membranes, diaphragms
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D17/00—Constructional parts, or assemblies thereof, of cells for electrolytic coating
    • C25D17/10—Electrodes, e.g. composition, counter electrode
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D21/00—Processes for servicing or operating cells for electrolytic coating
    • C25D21/06—Filtering particles other than ions
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D21/00—Processes for servicing or operating cells for electrolytic coating
    • C25D21/10—Agitating of electrolytes; Moving of racks
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D21/00—Processes for servicing or operating cells for electrolytic coating
    • C25D21/16—Regeneration of process solutions
    • C25D21/18—Regeneration of process solutions of electrolytes
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00—Electroplating: Baths therefor
    • C25D3/02—Electroplating: Baths therefor from solutions
    • C25D3/56—Electroplating: Baths therefor from solutions of alloys
    • C25D3/562—Electroplating: Baths therefor from solutions of alloys containing more than 50% by weight of iron or nickel or cobalt
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00—Electroplating: Baths therefor
    • C25D3/02—Electroplating: Baths therefor from solutions
    • C25D3/56—Electroplating: Baths therefor from solutions of alloys
    • C25D3/565—Electroplating: Baths therefor from solutions of alloys containing more than 50% by weight of zinc
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D17/00—Constructional parts, or assemblies thereof, of cells for electrolytic coating
    • C25D17/06—Suspending or supporting devices for articles to be coated

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

Abstract

To provide a zinc-based plating apparatus in which zinc ion concentration is prevented from increasing when an anode electrode is soluble, and a production method of a zinc-based plated member using the zinc-based plating apparatus.SOLUTION: A zinc-based plating apparatus 100 comprises: a plating tank 10 that can accommodate a plating solution PE; a first diaphragm tank 20 that includes a first diaphragm 21 having a first ion-exchange membrane, in which a first electrolyte can be accommodated; a cathode holding member 30 for electrolyzing, on a cathode, a to-be-plated member that contacts the plating solution inside the plating tank, when used; and a first anode holding member 40 for electrolyzing, on an anode, a soluble zinc-containing member 41 that contacts the first electrolyte inside the first diaphragm tank, when used. The first diaphragm tank is arranged so that the first electrolyte contacts one surface of the first diaphragm and the plating solution contacts the other surface of the first diaphragm, when used.SELECTED DRAWING: Figure 1

Description

本発明は、亜鉛系めっき装置および亜鉛系めっき部材の製造方法に関する。 The present invention relates to a zinc-based plating apparatus and a method for manufacturing a zinc-based plating member.

特許文献１には、陰極と陽極を備えたアルカリ亜鉛合金電気めっき浴において通電することを含む亜鉛合金電気めっき方法であって、陰極を含む陰極領域と陽極を含む陽極領域とが通電可能な電解液ゲルを含むセパレータで互いに分離されている、亜鉛合金電気めっき方法が記載されている。 Patent Document 1 is a zinc alloy electroplating method including energizing in an alkali-zinc alloy electroplating bath provided with a cathode and an anode, wherein the cathode region including the cathode and the anode region including the anode can be energized. Described are zinc alloy electroplating methods that are separated from each other by a separator containing a liquid gel.

特許文献２には、亜鉛−ニッケル皮膜電着用の、アノード（２）及びカソード（３）を有するアルカリ性めっき浴槽（１）において、該アノード（２）は、イオン交換膜（６）によりアルカリ性電解液（めっき浴）から隔離されている、ことを特徴とするめっき浴槽が記載されている。 In Patent Document 2, in an alkaline plating bath (1) having an anode (2) and a cathode (3), which is electrically worn with a zinc-nickel film, the anode (2) is an alkaline electrolyte solution by an ion exchange membrane (6). A plating bath characterized by being isolated from (plating bath) is described.

特許第５８３０２０２号公報Japanese Patent No. 5830202 特許第４７１６５６８号公報Japanese Patent No. 4716568

本発明は、陽極が溶解性である場合に亜鉛イオン濃度が高まりにくい亜鉛系めっき装置およびかかる亜鉛系めっき装置を用いた亜鉛系めっき部材の製造方法を提供する。 The present invention provides a zinc-based plating apparatus in which the zinc ion concentration does not easily increase when the anode is soluble, and a method for manufacturing a zinc-based plating member using such a zinc-based plating apparatus.

（１）亜鉛系めっき部材を製造するための亜鉛系めっき装置であって、めっき液を収容可能なめっき槽と、第１電解液を収容可能であって、第１イオン交換膜を含む第１隔膜を有する第１隔膜槽と、使用時に前記めっき槽の内部で前記めっき液に接触する被めっき部材を陰極電解するための陰極保持部材と、使用時に前記第１隔膜槽の内部で前記第１電解液に接触する溶解性亜鉛含有部材を陽極電解するための第１陽極保持部材と、を備え、使用時に前記第１隔膜の一方の面に前記第１電解液が接し前記第１隔膜の他方の面に前記めっき液が接するように、前記第１隔膜槽は配置されることを特徴とする亜鉛系めっき装置。
（２）前記めっき液は酸性である、上記（１）に記載の亜鉛系めっき装置。
（３）前記第１イオン交換膜は陽イオン交換膜を含む、上記（１）または上記（２）に記載の亜鉛系めっき装置。
（４）前記第１イオン交換膜は陰イオン交換膜を含む、上記（１）から上記（３）のいずれかに記載の亜鉛系めっき装置。
（５）前記第１陽極保持部材により保持される前記溶解性亜鉛含有部材をさらに備える、上記（１）から上記（４）のいずれかに記載の亜鉛系めっき装置。
（６）使用時に前記めっき液と電気的に接続される溶解性金属含有部材を陽極電解するための第２陽極保持部材をさらに備える、上記（１）から上記（５）のいずれかに記載の亜鉛系めっき装置。
（７）前記第２陽極保持部材により保持される前記溶解性金属含有部材をさらに備える、上記（６）に記載の亜鉛系めっき装置。
（８）前記溶解性金属含有部材は、亜鉛よりも貴な金属を溶解性金属として含む、上記（６）または上記（７）に記載の亜鉛系めっき装置。
（９）使用時に前記溶解性金属含有部材がめっき液に接触するように、前記第２陽極保持部材は配置される、上記（６）から上記（８）のいずれかに記載の亜鉛系めっき装置。
（１０）第２電解液を収容可能であって、第２イオン交換膜を含む第２隔膜を有する第２隔膜槽をさらに備え、使用時に、前記第２隔膜槽の内部で前記溶解性金属含有部材と接する前記第２電解液が前記第２隔膜の一方の面に接し前記第２隔膜の他方の面に前記めっき液が接するように、前記第２隔膜槽は配置される、上記（６）から上記（９）のいずれかに記載の亜鉛系めっき装置。
（１１）前記第２イオン交換膜は陽イオン交換膜を含む、上記（１０）に記載の亜鉛系めっき装置。
（１２）前記第２イオン交換膜は陰イオン交換膜を含む、上記（１０）または上記（１１）に記載の亜鉛系めっき装置。
（１３）第１イオン交換膜を含む第１隔膜を有し第１電解液を収容する第１隔膜槽を、前記第１隔膜の一方の面に前記第１電解液が接し、めっき槽の内部に収容されるめっき液が前記第１隔膜の他方の面に接するように配置し、前記めっき槽内で前記めっき液に接触する被めっき部材を陰極電解するとともに、前記第１隔膜槽の内部で前記第１電解液に接触する溶解性亜鉛含有部材を陽極電解することを特徴とする亜鉛系めっき部材の製造方法。
（１４）前記めっき液は酸性である、上記（１３）に記載の亜鉛系めっき部材の製造方法。
（１５）前記第１イオン交換膜は陽イオン交換膜を含む、上記（１３）または上記（１４）に記載の亜鉛系めっき部材の製造方法。
（１６）前記第１イオン交換膜は陰イオン交換膜を含む、上記（１３）から上記（１５）のいずれかに記載の亜鉛系めっき部材の製造方法。
（１７）前記めっき槽内で前記めっき液に接触する溶解性金属含有部材を陽極電解する、上記（１３）から上記（１６）のいずれかに記載の亜鉛系めっき部材の製造方法。
（１８）第２イオン交換膜を含む第２隔膜を有し第２電解液を収容する第２隔膜槽を、前記第２隔膜の一方の面に前記第２電解液が接し、前記第２隔膜の他方の面に前記めっき液が接するように配置し、前記第２隔膜槽内で前記第２電解液に接触する溶解性金属含有部材を陽極電解する、上記（１３）から上記（１６）のいずれかに記載の亜鉛系めっき部材の製造方法。
（１９）前記第２イオン交換膜は陽イオン交換膜を含む、上記（１８）に記載の亜鉛系めっき部材の製造方法。
（２０）前記第２イオン交換膜は陰イオン交換膜を含む、上記（１８）または上記（１９）に記載の亜鉛系めっき部材の製造方法。
（２１）前記溶解性金属含有部材は、亜鉛よりも貴な金属を溶解性金属として含む、上記（１７）から上記（２０）のいずれかに記載の亜鉛系めっき部材の製造方法。 (1) A first zinc-based plating apparatus for manufacturing a zinc-based plating member, which includes a plating tank capable of accommodating a plating solution and a first electrolytic solution capable of accommodating a first ion exchange film. A first diaphragm tank having a diaphragm, a cathode holding member for cathode electrolysis of a member to be plated that comes into contact with the plating solution inside the plating tank during use, and the first inside the first diaphragm tank during use. A first anode holding member for anodic electrolysis of a soluble zinc-containing member in contact with an electrolytic solution is provided, and the first electrolytic solution comes into contact with one surface of the first diaphragm during use and the other of the first diaphragm. A zinc-based plating apparatus, wherein the first diaphragm tank is arranged so that the plating solution comes into contact with the surface of the plating solution.
(2) The zinc-based plating apparatus according to (1) above, wherein the plating solution is acidic.
(3) The zinc-based plating apparatus according to (1) or (2) above, wherein the first ion exchange membrane includes a cation exchange membrane.
(4) The zinc-based plating apparatus according to any one of (1) to (3) above, wherein the first ion exchange membrane includes an anion exchange membrane.
(5) The zinc-based plating apparatus according to any one of (1) to (4) above, further comprising the soluble zinc-containing member held by the first anode holding member.
(6) The above-mentioned (1) to (5), further comprising a second anode holding member for anodic electrolyzing a soluble metal-containing member that is electrically connected to the plating solution during use. Zinc plating equipment.
(7) The zinc-based plating apparatus according to (6) above, further comprising the soluble metal-containing member held by the second anode holding member.
(8) The zinc-based plating apparatus according to (6) or (7) above, wherein the soluble metal-containing member contains a metal nobler than zinc as a soluble metal.
(9) The zinc-based plating apparatus according to any one of (6) to (8) above, wherein the second anode holding member is arranged so that the soluble metal-containing member comes into contact with the plating solution during use. ..
(10) A second diaphragm tank capable of accommodating the second electrolytic solution and having a second diaphragm including a second ion exchange membrane is further provided, and the soluble metal is contained inside the second diaphragm tank at the time of use. The second diaphragm tank is arranged so that the second electrolytic solution in contact with the member is in contact with one surface of the second diaphragm and the plating solution is in contact with the other surface of the second diaphragm. The zinc-based plating apparatus according to any one of (9) above.
(11) The zinc-based plating apparatus according to (10) above, wherein the second ion exchange membrane includes a cation exchange membrane.
(12) The zinc-based plating apparatus according to (10) or (11) above, wherein the second ion exchange membrane includes an anion exchange membrane.
(13) The inside of the plating tank is the first diaphragm tank having the first diaphragm including the first ion exchange membrane and accommodating the first electrolytic solution, in which the first electrolytic solution is in contact with one surface of the first diaphragm. The plating solution contained in the first diaphragm is arranged so as to be in contact with the other surface of the first diaphragm, and the member to be plated that comes into contact with the plating liquid is catholyzed in the plating tank, and inside the first diaphragm tank. A method for producing a zinc-based plated member, which comprises anodic electrolyzing a soluble zinc-containing member in contact with the first electrolytic solution.
(14) The method for producing a zinc-based plating member according to (13) above, wherein the plating solution is acidic.
(15) The method for producing a zinc-based plated member according to (13) or (14) above, wherein the first ion exchange membrane includes a cation exchange membrane.
(16) The method for producing a zinc-based plated member according to any one of (13) to (15) above, wherein the first ion exchange membrane includes an anion exchange membrane.
(17) The method for producing a zinc-based plating member according to any one of (13) to (16) above, wherein the soluble metal-containing member in contact with the plating solution is electrolyzed in the plating tank.
(18) The second electrolytic solution is in contact with one surface of the second diaphragm in a second diaphragm tank having a second diaphragm including a second ion exchange membrane and accommodating the second electrolytic solution, and the second electrolyte is in contact with the second diaphragm. The above (13) to (16), wherein the plating solution is arranged so as to be in contact with the other surface of the above, and the soluble metal-containing member in contact with the second electrolytic solution is electrolyzed in the second diaphragm tank. The method for manufacturing a zinc-based plated member according to any one.
(19) The method for producing a zinc-based plated member according to (18) above, wherein the second ion exchange membrane includes a cation exchange membrane.
(20) The method for producing a zinc-based plated member according to (18) or (19) above, wherein the second ion exchange membrane includes an anion exchange membrane.
(21) The method for producing a zinc-based plated member according to any one of (17) to (20) above, wherein the soluble metal-containing member contains a metal nobler than zinc as a soluble metal.

本発明によれば、陽極が溶解性である場合に亜鉛イオン濃度が高まりにくい亜鉛系めっき装置およびかかる亜鉛系めっき装置を用いた亜鉛系めっき部材の製造方法が提供される。 According to the present invention, there is provided a zinc-based plating apparatus in which the zinc ion concentration is unlikely to increase when the anode is soluble, and a method for manufacturing a zinc-based plating member using such a zinc-based plating apparatus.

本発明の第一実施形態に係る亜鉛系めっき装置の説明図である。It is explanatory drawing of the zinc-based plating apparatus which concerns on 1st Embodiment of this invention. 本発明の第二実施形態に係る亜鉛系めっき装置の説明図である。It is explanatory drawing of the zinc-based plating apparatus which concerns on 2nd Embodiment of this invention.

以下、本発明の実施形態について説明する。 Hereinafter, embodiments of the present invention will be described.

図１は、本発明の第一実施形態に係る亜鉛系めっき装置の説明図である。第一実施形態に係る亜鉛系めっき装置１００は、亜鉛系めっき部材を製造するためのものである。亜鉛系めっきとは、亜鉛めっきおよび亜鉛合金めっきの総称である。亜鉛合金めっきの具体例として、亜鉛ニッケルめっきが例示される。 FIG. 1 is an explanatory view of a zinc-based plating apparatus according to the first embodiment of the present invention. The zinc-based plating apparatus 100 according to the first embodiment is for manufacturing a zinc-based plating member. Zinc-based plating is a general term for zinc plating and zinc alloy plating. As a specific example of zinc alloy plating, zinc nickel plating is exemplified.

亜鉛系めっき装置１００はめっき槽１０、第１隔膜槽２０、陰極保持部材３０、および第１陽極保持部材４０を備える。 The zinc-based plating apparatus 100 includes a plating tank 10, a first diaphragm tank 20, a cathode holding member 30, and a first anode holding member 40.

めっき槽１０は、めっき液ＰＥを収容可能であって、図１ではめっき液ＰＥがめっき槽１０の内部に入っている。めっき槽１０を構成する材料の具体例としてポリプロピレンが挙げられる。めっき槽１０には、めっき液ＰＥを撹拌するための撹拌装置が設けられていてもよいし、めっき液ＰＥに生成する不溶性物質を除去するためのフィルターが設けられていてもよい。めっき槽１０には、めっき液ＰＥの撹拌と不溶性物質の除去とを行うために循環ポンプが設けられていてもよい。 The plating tank 10 can accommodate the plating solution PE, and in FIG. 1, the plating solution PE is inside the plating tank 10. Polypropylene is a specific example of the material constituting the plating tank 10. The plating tank 10 may be provided with a stirring device for stirring the plating solution PE, or may be provided with a filter for removing insoluble substances generated in the plating solution PE. The plating tank 10 may be provided with a circulation pump for stirring the plating solution PE and removing insoluble substances.

めっき液ＰＥの組成は、亜鉛系めっきの種類に応じて適宜設定される。具体的な一例として、めっき液ＰＥは酸性である。すなわち、本実施形態において、めっき液ＰＥは、酸性の亜鉛系めっき液である。本明細書において、亜鉛系めっき液とは、亜鉛元素を含むイオンを含有する電解液であって、陰極電解された被めっき部材３１に亜鉛を含むめっき膜を形成可能な液体を意味する。なお、亜鉛系めっき液には不溶成分が含まれていて、分散液の状態であってもよい。 The composition of the plating solution PE is appropriately set according to the type of zinc-based plating. As a specific example, the plating solution PE is acidic. That is, in the present embodiment, the plating solution PE is an acidic zinc-based plating solution. In the present specification, the zinc-based plating solution means an electrolytic solution containing ions containing zinc elements and capable of forming a zinc-containing plating film on the member 31 to be plated that has been catholy electrolyzed. The zinc-based plating solution contains an insoluble component and may be in the state of a dispersion liquid.

第１隔膜槽２０は、第１電解液Ｅ１を収容可能であって、図１では第１電解液Ｅ１が第１隔膜槽２０の内部に入っている。第１隔膜槽２０は、第１イオン交換膜を含む第１隔膜２１を有する。第１イオン交換膜は、陽イオン交換膜を含んでいてもよく、陰イオン交換膜を含んでいてもよい。後述するように、第１イオン交換膜は、陽イオン交換膜を含んでいることが好ましい場合がある。 The first diaphragm tank 20 can accommodate the first electrolytic solution E1, and in FIG. 1, the first electrolytic solution E1 is inside the first diaphragm tank 20. The first diaphragm tank 20 has a first diaphragm 21 including a first ion exchange membrane. The first ion exchange membrane may include a cation exchange membrane or may contain an anion exchange membrane. As will be described later, the first ion exchange membrane may preferably contain a cation exchange membrane.

第一実施形態に係る亜鉛系めっき装置１００では、第１隔膜槽２０はめっき槽１０の内部に位置し、第１隔膜２１の一方（第１隔膜槽２０の内側）の面に第１電解液Ｅ１が接し、第１隔膜２１の他方（第１隔膜槽２０の外側）の面にめっき液ＰＥが接するように、第１隔膜槽２０は配置されている。 In the zinc-based plating apparatus 100 according to the first embodiment, the first diaphragm tank 20 is located inside the plating tank 10, and the first electrolytic solution is placed on one surface of the first diaphragm 21 (inside the first diaphragm tank 20). The first diaphragm tank 20 is arranged so that E1 is in contact with the plating solution PE and the plating solution PE is in contact with the other surface of the first diaphragm 21 (outside of the first diaphragm tank 20).

第１隔膜槽２０を構成する材料の具体例としてポリプロピレンが挙げられる。第１隔膜槽２０には、その内部の第１電解液Ｅ１を撹拌するための撹拌装置が設けられていてもよいし、第１電解液Ｅ１に生成する不溶性物質を除去するためのフィルターが設けられていてもよい。第１隔膜槽２０には、第１電解液Ｅ１の撹拌と不溶性物質の除去とを行うために循環ポンプが設けられていてもよい。 Polypropylene is a specific example of the material constituting the first diaphragm tank 20. The first diaphragm tank 20 may be provided with a stirring device for stirring the first electrolytic solution E1 inside thereof, or a filter for removing insoluble substances generated in the first electrolytic solution E1. It may have been. The first diaphragm tank 20 may be provided with a circulation pump for stirring the first electrolytic solution E1 and removing insoluble substances.

本実施形態では、めっき槽１０の内部に第１隔膜槽２０が配置されているが、めっき槽１０の内部の一部が仕切られて、その仕切りに第１隔膜２１が設けられていてもよい。この場合には、仕切られた部分の内側が第１隔膜槽２０となってその内部に第１電解液Ｅ１が位置し、めっき槽１０の内部において仕切られた部分の外側にめっき液ＰＥが位置すればよい。 In the present embodiment, the first diaphragm tank 20 is arranged inside the plating tank 10, but a part of the inside of the plating tank 10 may be partitioned and the first diaphragm 21 may be provided in the partition. .. In this case, the inside of the partitioned portion becomes the first diaphragm tank 20, the first electrolytic solution E1 is located inside the first diaphragm tank 20, and the plating solution PE is located outside the partitioned portion inside the plating tank 10. do it.

陰極保持部材３０は、使用時にめっき槽１０の内部でめっき液ＰＥに接触する被めっき部材３１を陰極電解するためのものである。すなわち、陰極保持部材３０は、被めっき部材３１を保持する機能と被めっき部材３１に陰極電解電流を流す機能とを有する。陰極保持部材３０の形状は、保持する被めっき部材３１の形状に応じて適宜設定される。図１では、陰極保持部材３０は、板状の被めっき部材３１を挟持するクリップの形状を有する。陰極保持部材３０は被めっき部材３１を陰極電解できるように、電源装置６０の陰極端子６２に配線を介して接続されている。 The cathode holding member 30 is for cathodic electrolysis of the member 31 to be plated that comes into contact with the plating solution PE inside the plating tank 10 during use. That is, the cathode holding member 30 has a function of holding the member to be plated 31 and a function of passing a cathode electrolytic current through the member 31 to be plated. The shape of the cathode holding member 30 is appropriately set according to the shape of the member to be plated 31 to be held. In FIG. 1, the cathode holding member 30 has the shape of a clip that sandwiches the plate-shaped member to be plated 31. The cathode holding member 30 is connected to the cathode terminal 62 of the power supply device 60 via wiring so that the member 31 to be plated can be subjected to cathode electrolysis.

なお、本明細書において、陰極電解は、陽極電解の電位よりも相対的に負電位で電解されることを意味し、接地電位との関係では相対的に、正電位であってもよいし、負電位であってもよい。同様に、陽極電解は、陰極電解の電位よりも相対的に正電位で電解されることを意味し、接地電位との関係では相対的に、正電位であってもよいし、負電位であってもよい。 In this specification, cathode electrolysis means that electrolysis is performed at a negative potential relative to the potential of anodic electrolysis, and may be a positive potential relative to the ground potential. It may be a negative potential. Similarly, anodic electrolysis means that electrolysis is performed at a positive potential relative to the potential of cathodic electrolysis, and in relation to the ground potential, it may be a positive potential or a negative potential. You may.

第１陽極保持部材４０は、使用時に第１隔膜槽の内部で第１電解液Ｅ１に接触する溶解性亜鉛含有部材４１を陽極電解するためのものである。すなわち、第１陽極保持部材４０は、溶解性亜鉛含有部材４１を保持する機能と溶解性亜鉛含有部材４１に陽極電解電流を流す機能とを有する。第１陽極保持部材４０の形状は、保持する溶解性亜鉛含有部材４１の形状に応じて適宜設定される。図１では、第１陽極保持部材４０は、複数の亜鉛のインゴット（塊）からなる溶解性亜鉛含有部材４１を保持するかごの形状を有する。第１陽極保持部材４０は溶解性亜鉛含有部材４１を陽極電解できるように、電源装置６０の陽極端子６１に配線を介して接続されている。 The first anode holding member 40 is for anodic electrolyzing the soluble zinc-containing member 41 that comes into contact with the first electrolytic solution E1 inside the first diaphragm tank during use. That is, the first anode holding member 40 has a function of holding the soluble zinc-containing member 41 and a function of passing an anode electrolytic current through the soluble zinc-containing member 41. The shape of the first anode holding member 40 is appropriately set according to the shape of the soluble zinc-containing member 41 to be held. In FIG. 1, the first anode holding member 40 has a cage shape for holding a soluble zinc-containing member 41 composed of a plurality of zinc ingots (lumps). The first anode holding member 40 is connected to the anode terminal 61 of the power supply device 60 via wiring so that the soluble zinc-containing member 41 can be electrolyzed.

第１電解液Ｅ１は亜鉛元素を含むイオンを含有する電解液であって、溶解性亜鉛含有部材４１が陽極電解されたときに、溶解性亜鉛含有部材４１に含まれる亜鉛をイオンとして溶解することができる。なお、第１電解液Ｅ１には不溶成分が含まれていて、分散液の状態であってもよい。 The first electrolytic solution E1 is an electrolytic solution containing ions containing zinc elements, and when the soluble zinc-containing member 41 is electrolyzed, the zinc contained in the soluble zinc-containing member 41 is dissolved as ions. Can be done. The first electrolytic solution E1 may contain an insoluble component and may be in the state of a dispersion liquid.

亜鉛系めっき装置１００は、使用時にめっき液ＰＥと電気的に接続される溶解性金属含有部材５１を陽極電解するための第２陽極保持部材５０をさらに備える。すなわち、第２陽極保持部材５０は、溶解性金属含有部材５１を保持する機能と溶解性金属含有部材５１に陽極電解電流を流す機能とを有する。第２陽極保持部材５０の形状は、保持する溶解性金属含有部材５１の形状に応じて適宜設定される。図１では、第１陽極保持部材４０は、複数のニッケルのインゴット（塊）からなる溶解性金属含有部材５１を保持するかごの形状を有する。第２陽極保持部材５０は溶解性金属含有部材５１を陽極電解できるように、電源装置６０の陽極端子６１に配線を介して接続されている。 The zinc-based plating apparatus 100 further includes a second anode holding member 50 for anodic electrolyzing the soluble metal-containing member 51 that is electrically connected to the plating solution PE during use. That is, the second anode holding member 50 has a function of holding the soluble metal-containing member 51 and a function of passing an anode electrolytic current through the soluble metal-containing member 51. The shape of the second anode holding member 50 is appropriately set according to the shape of the soluble metal-containing member 51 to be held. In FIG. 1, the first anode holding member 40 has the shape of a cage that holds a soluble metal-containing member 51 composed of a plurality of nickel ingots (lumps). The second anode holding member 50 is connected to the anode terminal 61 of the power supply device 60 via wiring so that the soluble metal-containing member 51 can be electrolyzed.

溶解性金属含有部材５１は、第２陽極保持部材５０に保持されてめっき槽１０の内部に位置し、めっき液ＰＥに直接的に接することにより、めっき液ＰＥと電気的に接続されている。溶解性金属含有部材５１は、亜鉛合金めっきにおける合金元素の供給源となり得る。上記のように、溶解性金属含有部材５１が複数のニッケルのインゴット（塊）からなる場合には、亜鉛合金めっきは亜鉛ニッケルめっきとなることができる。溶解性金属含有部材５１は、上記のニッケルのように、亜鉛よりも貴な金属を溶解性金属として含んでいてもよい。 The soluble metal-containing member 51 is held by the second anode holding member 50 and is located inside the plating tank 10, and is electrically connected to the plating solution PE by directly contacting the plating solution PE. The soluble metal-containing member 51 can be a source of alloying elements in zinc alloy plating. As described above, when the soluble metal-containing member 51 is composed of a plurality of nickel ingots (lumps), the zinc alloy plating can be zinc nickel plating. The soluble metal-containing member 51 may contain a metal nobler than zinc as the soluble metal, such as nickel described above.

なお、図１では、第１陽極保持部材４０と第２陽極保持部材５０とは共通の陽極端子６１に接続されているが、これに限定されない。第１陽極保持部材４０の陽極電解電位と第２陽極保持部材５０の陽極電解電位とが異なっていてもよい。 In FIG. 1, the first anode holding member 40 and the second anode holding member 50 are connected to a common anode terminal 61, but the present invention is not limited to this. The anode electrolysis potential of the first anode holding member 40 and the anode electrolysis potential of the second anode holding member 50 may be different.

図２は、本発明の第二実施形態に係る亜鉛系めっき装置の説明図である。第二実施形態に係る亜鉛系めっき装置１０１は、基本構成は第一実施形態に係る亜鉛系めっき装置１００に等しい。第一実施形態に係る亜鉛系めっき装置１００と対比したときの第二実施形態に係る亜鉛系めっき装置１０１の相違点は、第２陽極保持部材５０が、第２電解液Ｅ２を収容する第２隔膜槽７０の内部に位置していることである。 FIG. 2 is an explanatory view of a zinc-based plating apparatus according to a second embodiment of the present invention. The zinc-based plating apparatus 101 according to the second embodiment has the same basic configuration as the zinc-based plating apparatus 100 according to the first embodiment. The difference between the zinc-based plating apparatus 101 according to the second embodiment when compared with the zinc-based plating apparatus 100 according to the first embodiment is that the second anode holding member 50 accommodates the second electrolytic solution E2. It is located inside the diaphragm tank 70.

すなわち、亜鉛系めっき装置１０１は、第２イオン交換膜を含む第２隔膜７１を有する第２隔膜槽７０を備える。第２隔膜槽７０は、第２隔膜７１の一方（第２隔膜槽７０の内側）の面に第２電解液Ｅ２が接し、第２隔膜７１の他方（第２隔膜槽７０の外側）の面にめっき液ＰＥが接するように、配置されている。第２電解液Ｅ２は、第２隔膜槽７０の内部で、第２陽極保持部材５０に保持される溶解性金属含有部材５１と接する。 That is, the zinc-based plating apparatus 101 includes a second diaphragm tank 70 having a second diaphragm 71 including a second ion exchange membrane. In the second diaphragm tank 70, the second electrolytic solution E2 is in contact with one surface of the second diaphragm 71 (inside the second diaphragm tank 70), and the other surface of the second diaphragm 71 (outside the second diaphragm tank 70). The plating solution PE is arranged so as to be in contact with the surface. The second electrolytic solution E2 comes into contact with the soluble metal-containing member 51 held by the second anode holding member 50 inside the second diaphragm tank 70.

第２隔膜槽７０を構成する材料の具体例としてポリプロピレンが挙げられる。第２隔膜槽７０には、その内部の第２電解液Ｅ２を撹拌するための撹拌装置が設けられていてもよいし、第２電解液Ｅ２に生成する不溶性物質を除去するためのフィルターが設けられていてもよい。第２隔膜槽７０には、第２電解液Ｅ２の撹拌と不溶性物質の除去とを行うために循環ポンプが設けられていてもよい。 Polypropylene is a specific example of the material constituting the second diaphragm tank 70. The second diaphragm tank 70 may be provided with a stirring device for stirring the second electrolytic solution E2 inside thereof, or a filter for removing insoluble substances generated in the second electrolytic solution E2. It may have been. The second diaphragm tank 70 may be provided with a circulation pump for stirring the second electrolytic solution E2 and removing insoluble substances.

本実施形態では、めっき槽１０の内部に第２隔膜槽７０が配置されているが、めっき槽１０の内部の一部が仕切られて、その仕切りに第２隔膜７１が設けられていてもよい。この場合には、仕切られた部分の内側が第２隔膜槽７０となってその内部に第２電解液Ｅ２が位置し、めっき槽１０の内部において仕切られた部分の外側にめっき液ＰＥが位置すればよい。 In the present embodiment, the second diaphragm tank 70 is arranged inside the plating tank 10, but a part of the inside of the plating tank 10 may be partitioned and the second diaphragm 71 may be provided in the partition. .. In this case, the inside of the partitioned portion becomes the second diaphragm tank 70, the second electrolytic solution E2 is located inside the second diaphragm tank 70, and the plating solution PE is located outside the partitioned portion inside the plating tank 10. do it.

第２電解液Ｅ２は電解液であって、溶解性金属含有部材５１が陽極電解されたときに、溶解性金属含有部材５１に含まれる金属をイオンとして溶解することができる。なお、第２電解液Ｅ２には不溶成分が含まれていて、分散液の状態であってもよい。 The second electrolytic solution E2 is an electrolytic solution, and when the soluble metal-containing member 51 is anoly electrolyzed, the metal contained in the soluble metal-containing member 51 can be dissolved as an ion. The second electrolytic solution E2 may contain an insoluble component and may be in the state of a dispersion liquid.

第２イオン交換膜は、陽イオン交換膜を含んでいてもよいし、陰イオン交換膜を含んでいてもよい。第２イオン交換膜は、第１イオン交換膜と等しい構成を有していてもよいし、異なる構成を有していてもよい。 The second ion exchange membrane may include a cation exchange membrane or an anion exchange membrane. The second ion exchange membrane may have the same structure as the first ion exchange membrane, or may have a different structure.

以上説明した実施形態は、本発明の理解を容易にするために記載されたものであって、本発明を限定するために記載されたものではない。したがって、上記実施形態に開示された各要素は、本発明の技術的範囲に属する全ての設計変更や均等物をも含む趣旨である。例えば、第１隔膜槽２０は構成の異なる第１隔膜２１を複数有していてもよく、第２隔膜槽７０は構成の異なる第２隔膜７１を複数有していてもよい。 The embodiments described above are described for facilitating the understanding of the present invention, and are not described for limiting the present invention. Therefore, each element disclosed in the above embodiment is intended to include all design changes and equivalents belonging to the technical scope of the present invention. For example, the first diaphragm tank 20 may have a plurality of first diaphragms 21 having different configurations, and the second diaphragm tank 70 may have a plurality of second diaphragms 71 having different configurations.

以下、本発明の効果を実施例に基づいて説明するが、本発明はこれに限定されるものではない。 Hereinafter, the effects of the present invention will be described based on examples, but the present invention is not limited thereto.

（実施例１）
表１に示される組成の酸性亜鉛ニッケルめっき液を用意した。 (Example 1)
An acidic zinc-nickel plating solution having the composition shown in Table 1 was prepared.

Figure 2021085068
Figure 2021085068

図１に示される亜鉛系めっき装置１００を用いて、上記の酸性亜鉛ニッケルめっき液をめっき液ＰＥとしてめっき槽１０に入れ、次のいずれかの電解液を第１電解液Ｅ１（内部液）として第１隔膜槽２０に入れた。
（電解液Ａ）塩化亜鉛濃度５０ｇ／Ｌ
（電解液Ｂ）塩化亜鉛濃度５００ｇ／Ｌ
（電解液Ｃ）塩化亜鉛濃度０ｇ／Ｌ Using the zinc-based plating apparatus 100 shown in FIG. 1, the above acidic zinc nickel plating solution is put into the plating tank 10 as the plating solution PE, and any of the following electrolytic solutions is used as the first electrolytic solution E1 (internal solution). It was placed in the first diaphragm tank 20.
(Electrolytic solution A) Zinc chloride concentration 50 g / L
(Electrolytic solution B) Zinc chloride concentration 500 g / L
(Electrolytic solution C) Zinc chloride concentration 0 g / L

第１隔膜槽２０の第１隔膜２１として、表２に示されるいずれかのイオン交換膜を用いた。

Figure 2021085068
As the first diaphragm 21 of the first diaphragm tank 20, any ion exchange membrane shown in Table 2 was used.
Figure 2021085068

表３に示される条件でめっきを行った。なお、表３中の通電時間の単位は時間である。

Figure 2021085068
Plating was performed under the conditions shown in Table 3. The unit of energization time in Table 3 is time.
Figure 2021085068

表３に示されるように、第１隔膜槽２０が設けられていない場合（実験Ｎｏ．１）には、通電することにより、めっき液ＰＥにおける亜鉛濃度は高くなった（４０．２ｇ／Ｌ）。 As shown in Table 3, when the first diaphragm tank 20 was not provided (Experiment No. 1), the zinc concentration in the plating solution PE was increased by energizing (40.2 g / L). ..

これに対し、アニオン膜（陰イオン交換膜）を第１隔膜２１として有する第１隔膜槽２０が設けられ第１電解液Ｅ１（内部液）の亜鉛濃度が０ｇ／Ｌ（電解液Ｃ）の場合（実験Ｎｏ．２）には、通電によるめっき液ＰＥにおける亜鉛濃度の上昇は抑えられた（２０．５ｇ／Ｌ）。 On the other hand, when the first diaphragm tank 20 having an anion membrane (anion exchange membrane) as the first diaphragm 21 is provided and the zinc concentration of the first electrolytic solution E1 (internal solution) is 0 g / L (electrolyte solution C). In (Experiment No. 2), the increase in zinc concentration in the plating solution PE due to energization was suppressed (20.5 g / L).

カチオン膜（陽イオン交換膜）を第１隔膜２１として有する第１隔膜槽２０が設けられ第１電解液Ｅ１（内部液）の亜鉛濃度が２５ｇ／Ｌ（電解液Ａ）の場合（実験Ｎｏ．３）には、通電によるめっき液ＰＥにおける亜鉛濃度の上昇は抑えられた（３０．１ｇ／Ｌ）。 When the first diaphragm tank 20 having a cation membrane (cation exchange membrane) as the first diaphragm 21 is provided and the zinc concentration of the first electrolytic solution E1 (internal solution) is 25 g / L (electrolyte solution A) (Experiment No. In 3), the increase in zinc concentration in the plating solution PE due to energization was suppressed (30.1 g / L).

カチオン膜（陽イオン交換膜）を第１隔膜２１として有する第１隔膜槽２０が設けられ第１電解液Ｅ１（内部液）の亜鉛濃度が５００ｇ／Ｌ（電解液Ａ）の場合（実験Ｎｏ．４）には、通電によるめっき液ＰＥにおける亜鉛濃度の上昇は抑えられた（３２．５ｇ／Ｌ）。 When the first diaphragm tank 20 having a cation membrane (cation exchange membrane) as the first diaphragm 21 is provided and the zinc concentration of the first electrolytic solution E1 (internal solution) is 500 g / L (electrolyte solution A) (Experiment No. In 4), the increase in zinc concentration in the plating solution PE due to energization was suppressed (32.5 g / L).

実験Ｎｏ．３および実験Ｎｏ．４と陽イオン交換膜の種類だけを相違させた場合（実験Ｎｏ．５、実験Ｎｏ．６）には、実験Ｎｏ．３および実験Ｎｏ．４と同様に、通電によるめっき液ＰＥにおける亜鉛濃度の上昇は抑えられた（実験Ｎｏ．５：３４．０ｇ／Ｌ、実験Ｎｏ．６：３４．５ｇ／Ｌ）。 Experiment No. 3 and Experiment No. When only the type of the cation exchange membrane is different from that of No. 4 (Experiment No. 5 and Experiment No. 6), the experiment No. 3 and Experiment No. Similar to No. 4, the increase in zinc concentration in the plating solution PE due to energization was suppressed (Experiment No. 5: 34.0 g / L, Experiment No. 6: 34.5 g / L).

実験Ｎｏ．４の条件において、第２隔膜槽７０の効果について確認した。実験Ｎｏ．４の条件において通電後のニッケル濃度を測定すると、通電前の２０．０ｇ／Ｌよりも増加して、２１．３ｇ／Ｌとなった。内部のニッケル濃度が２０ｇ／Ｌの第２電解液Ｅ２が入った第２隔膜槽７０を用いた結果を表４に示す。第２隔膜７１がアニオン膜（陰イオン交換膜）である場合（実験Ｎｏ．７）のニッケル濃度は１６．７ｇ／Ｌとなり、第２隔膜７１がカチオン膜（陽イオン交換膜）である場合（実験Ｎｏ．８）のニッケル濃度は１８．５ｇ／Ｌとなって、いずれの場合も第２隔膜槽７０を用いない場合よりもニッケル濃度の上昇を抑制することができた。 Experiment No. The effect of the second diaphragm tank 70 was confirmed under the condition of 4. Experiment No. When the nickel concentration after energization was measured under the condition of 4, it increased from 20.0 g / L before energization to 21.3 g / L. Table 4 shows the results of using the second diaphragm tank 70 containing the second electrolytic solution E2 having an internal nickel concentration of 20 g / L. When the second diaphragm 71 is an anion membrane (anion exchange membrane) (Experiment No. 7), the nickel concentration is 16.7 g / L, and when the second diaphragm 71 is a cation membrane (cation exchange membrane) ( The nickel concentration in Experiment No. 8) was 18.5 g / L, and in each case, the increase in nickel concentration could be suppressed as compared with the case where the second diaphragm tank 70 was not used.

Figure 2021085068
Figure 2021085068

１００、１０１ ：亜鉛系めっき装置
１０ ：めっき槽
２０ ：第１隔膜槽
２１ ：第１隔膜
３０ ：陰極保持部材
３１ ：被めっき部材
４０ ：第１陽極保持部材
４１ ：溶解性亜鉛含有部材
５０ ：第２陽極保持部材
５１ ：溶解性金属含有部材
６０ ：電源装置
６１ ：陽極端子
６２ ：陰極端子
７０ ：第２隔膜槽
７１ ：第２隔膜
Ｅ１ ：第１電解液
Ｅ２ ：第２電解液
ＰＥ ：めっき液 100, 101: Zinc-based plating apparatus 10: Plating tank 20: First diaphragm tank 21: First diaphragm 30: Cathode holding member 31: Plated member 40: First anode holding member 41: Soluble zinc-containing member 50: First 2 Anode holding member 51: Soluble metal-containing member 60: Power supply device 61: Anode terminal 62: Cathode terminal 70: Second diaphragm tank 71: Second diaphragm E1: First electrolyte E2: Second electrolyte PE: Plating liquid

Claims (21)

亜鉛系めっき部材を製造するための亜鉛系めっき装置であって、
めっき液を収容可能なめっき槽と、
第１電解液を収容可能であって、第１イオン交換膜を含む第１隔膜を有する第１隔膜槽と、
使用時に前記めっき槽の内部で前記めっき液に接触する被めっき部材を陰極電解するための陰極保持部材と、
使用時に前記第１隔膜槽の内部で前記第１電解液に接触する溶解性亜鉛含有部材を陽極電解するための第１陽極保持部材と、
を備え、
使用時に前記第１隔膜の一方の面に前記第１電解液が接し前記第１隔膜の他方の面に前記めっき液が接するように、前記第１隔膜槽は配置されることを特徴とする亜鉛系めっき装置。 A zinc-based plating device for manufacturing zinc-based plating members.
A plating tank that can store the plating solution and
A first diaphragm tank capable of accommodating the first electrolyte and having a first diaphragm including a first ion exchange membrane,
A cathode holding member for cathodic electrolysis of a member to be plated that comes into contact with the plating solution inside the plating tank during use.
A first anode holding member for anodic electrolyzing a soluble zinc-containing member that comes into contact with the first electrolytic solution inside the first diaphragm tank during use.
With
Zinc is characterized in that the first diaphragm tank is arranged so that the first electrolytic solution comes into contact with one surface of the first diaphragm and the plating solution comes into contact with the other surface of the first diaphragm during use. System plating equipment. 前記めっき液は酸性である、請求項１に記載の亜鉛系めっき装置。 The zinc-based plating apparatus according to claim 1, wherein the plating solution is acidic. 前記第１イオン交換膜は陽イオン交換膜を含む、請求項１または請求項２に記載の亜鉛系めっき装置。 The zinc-based plating apparatus according to claim 1 or 2, wherein the first ion exchange membrane includes a cation exchange membrane. 前記第１イオン交換膜は陰イオン交換膜を含む、請求項１から請求項３のいずれか一項に記載の亜鉛系めっき装置。 The zinc-based plating apparatus according to any one of claims 1 to 3, wherein the first ion exchange membrane includes an anion exchange membrane. 前記第１陽極保持部材により保持される前記溶解性亜鉛含有部材をさらに備える、請求項１から請求項４のいずれか一項に記載の亜鉛系めっき装置。 The zinc-based plating apparatus according to any one of claims 1 to 4, further comprising the soluble zinc-containing member held by the first anode holding member. 使用時に前記めっき液と電気的に接続される溶解性金属含有部材を陽極電解するための第２陽極保持部材をさらに備える、請求項１から請求項５のいずれか一項に記載の亜鉛系めっき装置。 The zinc-based plating according to any one of claims 1 to 5, further comprising a second anode holding member for anodic electrolyzing a soluble metal-containing member electrically connected to the plating solution at the time of use. apparatus. 前記第２陽極保持部材により保持される前記溶解性金属含有部材をさらに備える、請求項６に記載の亜鉛系めっき装置。 The zinc-based plating apparatus according to claim 6, further comprising the soluble metal-containing member held by the second anode holding member. 前記溶解性金属含有部材は、亜鉛よりも貴な金属を溶解性金属として含む、請求項６または請求項７に記載の亜鉛系めっき装置。 The zinc-based plating apparatus according to claim 6 or 7, wherein the soluble metal-containing member contains a metal nobler than zinc as the soluble metal. 使用時に前記溶解性金属含有部材がめっき液に接触するように、前記第２陽極保持部材は配置される、請求項６から請求項８のいずれか一項に記載の亜鉛系めっき装置。 The zinc-based plating apparatus according to any one of claims 6 to 8, wherein the second anode holding member is arranged so that the soluble metal-containing member comes into contact with the plating solution during use. 第２電解液を収容可能であって、第２イオン交換膜を含む第２隔膜を有する第２隔膜槽をさらに備え、使用時に、前記第２隔膜槽の内部で前記溶解性金属含有部材と接する前記第２電解液が前記第２隔膜の一方の面に接し前記第２隔膜の他方の面に前記めっき液が接するように、前記第２隔膜槽は配置される、請求項６から請求項９のいずれか一項に記載の亜鉛系めっき装置。 A second diaphragm tank capable of accommodating the second electrolytic solution and having a second diaphragm including a second ion exchange membrane is further provided, and is in contact with the soluble metal-containing member inside the second diaphragm tank during use. The second diaphragm tank is arranged so that the second electrolytic solution is in contact with one surface of the second diaphragm and the plating solution is in contact with the other surface of the second diaphragm, claims 6 to 9. The zinc-based plating apparatus according to any one of the above. 前記第２イオン交換膜は陽イオン交換膜を含む、請求項１０に記載の亜鉛系めっき装置。 The zinc-based plating apparatus according to claim 10, wherein the second ion exchange membrane includes a cation exchange membrane. 前記第２イオン交換膜は陰イオン交換膜を含む、請求項１０または請求項１１に記載の亜鉛系めっき装置。 The zinc-based plating apparatus according to claim 10 or 11, wherein the second ion exchange membrane includes an anion exchange membrane. 第１イオン交換膜を含む第１隔膜を有し第１電解液を収容する第１隔膜槽を、前記第１隔膜の一方の面に前記第１電解液が接し、めっき槽の内部に収容されるめっき液が前記第１隔膜の他方の面に接するように配置し、
前記めっき槽内で前記めっき液に接触する被めっき部材を陰極電解するとともに、
前記第１隔膜槽の内部で前記第１電解液に接触する溶解性亜鉛含有部材を陽極電解すること
を特徴とする亜鉛系めっき部材の製造方法。 The first diaphragm tank having the first diaphragm including the first ion exchange membrane and accommodating the first electrolytic solution is housed inside the plating tank with the first electrolytic solution in contact with one surface of the first diaphragm. The plating solution is arranged so as to be in contact with the other surface of the first diaphragm.
In the plating tank, the member to be plated that comes into contact with the plating solution is cathodically electrolyzed, and at the same time,
A method for producing a zinc-based plated member, which comprises anodic electrolyzing a soluble zinc-containing member in contact with the first electrolytic solution inside the first diaphragm tank. 前記めっき液は酸性である、請求項１３に記載の亜鉛系めっき部材の製造方法。 The method for producing a zinc-based plating member according to claim 13, wherein the plating solution is acidic. 前記第１イオン交換膜は陽イオン交換膜を含む、請求項１３または請求項１４に記載の亜鉛系めっき部材の製造方法。 The method for producing a zinc-based plated member according to claim 13 or 14, wherein the first ion exchange membrane includes a cation exchange membrane. 前記第１イオン交換膜は陰イオン交換膜を含む、請求項１３から請求項１５のいずれか一項に記載の亜鉛系めっき部材の製造方法。 The method for producing a zinc-based plated member according to any one of claims 13 to 15, wherein the first ion exchange membrane includes an anion exchange membrane. 前記めっき槽内で前記めっき液に接触する溶解性金属含有部材を陽極電解する、請求項１３から請求項１６のいずれか一項に記載の亜鉛系めっき部材の製造方法。 The method for producing a zinc-based plating member according to any one of claims 13 to 16, wherein the soluble metal-containing member in contact with the plating solution is electrolyzed in the plating tank. 第２イオン交換膜を含む第２隔膜を有し第２電解液を収容する第２隔膜槽を、前記第２隔膜の一方の面に前記第２電解液が接し、前記第２隔膜の他方の面に前記めっき液が接するように配置し、
前記第２隔膜槽内で前記第２電解液に接触する溶解性金属含有部材を陽極電解する、請求項１３から請求項１６のいずれか一項に記載の亜鉛系めっき部材の製造方法。 A second diaphragm tank having a second diaphragm including a second ion exchange membrane and accommodating the second electrolyte solution is in contact with one surface of the second diaphragm and the second electrolyte solution is in contact with the other of the second diaphragm. Arranged so that the plating solution is in contact with the surface,
The method for producing a zinc-based plated member according to any one of claims 13 to 16, wherein the soluble metal-containing member in contact with the second electrolytic solution is electrolyzed in the second diaphragm tank. 前記第２イオン交換膜は陽イオン交換膜を含む、請求項１８に記載の亜鉛系めっき部材の製造方法。 The method for producing a zinc-based plated member according to claim 18, wherein the second ion exchange membrane includes a cation exchange membrane. 前記第２イオン交換膜は陰イオン交換膜を含む、請求項１８または請求項１９に記載の亜鉛系めっき部材の製造方法。 The method for producing a zinc-based plated member according to claim 18 or 19, wherein the second ion exchange membrane includes an anion exchange membrane. 前記溶解性金属含有部材は、亜鉛よりも貴な金属を溶解性金属として含む、請求項１７から請求項２０のいずれか一項に記載の亜鉛系めっき部材の製造方法。 The method for producing a zinc-based plated member according to any one of claims 17 to 20, wherein the soluble metal-containing member contains a metal nobler than zinc as the soluble metal.
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