The present technology includes methods for rinsing an electroplating apparatus, a component thereof, and/or a substrate. The method includes removing at least a portion of a bath solution having a first pH from an electroplating bath. The method includes filtering the removed bath solution through a nanofiltration membrane, forming a permeating containing a recycled rinse agent, and a retentate. The method includes transferring the recycled rinse agent to the one or more nozzles and rinsing the electroplating apparatus, component thereof, and/or substrate. The method includes where the recycled rinse agent is characterized by a second pH, where the second pH varies from the first pH by less than or about 5.

The invention relates to a method for the adjustment of the lightness L* of electrolytically deposited chromium-finishes on workpieces obtained by an electroplating bath comprising at least chromium(III)-ions and sulfur containing organic compounds, wherein the concentration of the sulfur containing organic compounds in the bath are adjusted by passing at least part of the bath composition through an activated carbon filter. Furthermore, the invention is directed to dark chrome coatings comprising a defined concentration gradient of deposited sulfur containing organic compounds.

The invention relates to a method for the adjustment of the lightness L* of electrolytically deposited chromium-finishes on workpieces obtained by an electroplating bath comprising at least chromium(III)-ions and sulfur containing organic compounds, wherein the concentration of the sulfur containing organic compounds in the bath are adjusted by passing at least part of the bath composition through an activated carbon filter. Furthermore, the invention is directed to dark chrome coatings comprising a defined concentration gradient of deposited sulfur containing organic compounds.

Systems and methods for tin antimony plating are provided. One plating method includes doping a tin (Sn) plating solution with antimony (Sb). One method also includes electroplating a component using the antimony-doped tin plating. The antimony-doped tin plating formed by one method includes between about 1% and about 3% antimony.

A non alpha controlled alloy that includes a metal and an alpha emitting material is utilized as a plating anode to selectively plate the metal upon a plating cathode. The metal may be selectively plated by pulse plating the non alpha controlled alloy with current control to suppress plating of the alpha emitting material upon the plating cathode. The metal may also be selectively plated by pulse plating the non alpha controlled alloy with potential control to suppress plating of the alpha emitting material upon the plating cathode. The metal may also be selectively plated by plating out the alpha emitting material upon a filtering cathode.

A non alpha controlled Tin including Tin and a trace amount of Polonium is utilized as a plating anode to selectively plate Tin upon a plating cathode. Tin may be selectively plated by pulse plating the non alpha controlled Tin with current control to suppress plating of Polonium upon the plating cathode. Tin may also be selectively plated by pulse plating the non alpha controlled Tin with potential control to suppress plating of Polonium upon the plating cathode. Tin may also be selectively plated by pulse and reverse plating to plate out Polonium upon a filtering cathode. Tin may also be selectively plated by plating out Polonium upon a filtering cathode within a concentrate. Tin may also be selectively plated by plating out purified Tin upon a filtering cathode, separating the purified Tin from the filtering cathode, and utilizing the purified Tin to plate Tin upon the plating cathode.

The invention relates to a system for the local surface treatment of an aeronautical part (1) to be treated.

Said system is characterised in that it comprises a plurality of containers (18, 19, 20, 21) each comprising a treatment product (22, 23, 24, 25), at least one bath enclosure (102a, 102b) suitable for delimiting a fluid-tight space (26a, 26b) between this bath enclosure (102a, 102b) and a portion (101a, 101b) of the part to be treated, and a controlled circuit (10) for supplying said fluid-tight space (26a, 26b) with treatment product (22, 23, 24, 25) the containers (18, 19, 20, 21) connecting at least this container (18, 19, 20, 21) to said fluid-tight space (26a, 26b) and comprising valves for managing the supply to the fluid-tight space by one or more containers from the plurality of containers.

An electro-chemical plating process begins with supplying a supercritical fluid into an electroplating solution to be deposited, and a bias is applied between a substrate and an electrode, which is located in the electroplating solution. The substrate is placed into the electroplating solution to deposit a material on the substrate.

An electro-chemical plating process begins with supplying a supercritical fluid into an electroplating solution to be deposited, and a bias is applied between a substrate and an electrode, which is located in the electroplating solution. The substrate is placed into the electroplating solution to deposit a material on the substrate.

A plating product fabrication method includes forming a first concentrate. The concentrate includes a Tin (Sn) species and a trace amount of Polonium (Po) species. The plating product fabrication method also includes creating a circuit between a filtering anode and a filtering cathode and reducing the Po species from the concentrate by plating Po upon the filtering cathode. In this manner, a purified Sn concentrate is formed. The purified Sn concentrate may be utilized to plate Sn upon a plating cathode. The purified Sn concentrate may be utilized to form purified Sn.