The present disclosure concerns an array of chemical and electrochemical treatment cells. The cells include electrochemical cells that individually include a plating tank, a power supply, and an anode. A flight bar for supporting a cathode is moved from one tank to another for treating and plating a cathode surface. Within an electrochemical tank, the power supply operates a circuit with metal ions being eroded from the anode and being deposited onto the cathode surface. A plating apparatus is configured to simultaneously provide mechanical support, a cathodic connection, and agitation to a cathode in a plating tank. The plating apparatus includes an agitator which rotates the cathode about a fixed pivot connection to provide motion along a lateral axis and a vertical axis.

In one example, a method to manufacture a magnetic sensor, comprises providing an electrolyte solution, submersing a substrate in the electrolyte solution, submersing a plurality of ingots in the electrolyte solution, wherein the ingots comprises a metal that is magnetic, and depositing the metal on the substrate by applying a voltage between the metal ingot and the substrate to result in magnetic alloy layer on the substrate. Other examples and related methods are also disclosed herein.

An apparatus and system for in-situ electropolishing and/or for in-situ electroforming a structural or functional reinforcement layer such as a sleeve of a selected metallic material on the internal surfaces of metallic tubular conduits are described. The apparatus and system can be employed on straight tubes, tube joints to different diameter tubes or face plates, tube elbows and other complex shapes encountered in piping systems. The apparatus includes components which can be independently manipulated and assembled on or near a degraded site and, after secured in place, form an electrolytic cell within the workpiece. The apparatus contains counter-electrodes which can be moved relative to the workpiece surface during the electroplating and/or electropolishing operation to provide flexibility in selecting and employing electropolishing process parameters and electroplating process parameters to design and optimize the surface roughness as well as the size, shape and properties of the electrodeposited reinforcing layer(s).

The embodiments herein relate to methods and apparatus for electroplating one or more materials onto a substrate. Typically, the embodiments herein utilize a channeled plate positioned near the substrate, creating a cross flow manifold between the channeled plate and substrate, and on the sides by a flow confinement ring. A seal may be provided between the bottom surface of a substrate holder and the top surface of an element below the substrate holder (e.g., the flow confinement ring). During plating, fluid enters the cross flow manifold through channels in the channeled plate, and through a cross flow inlet, then exits at the cross flow exit, positioned opposite the cross flow inlet. The apparatus may switch between a sealed state and an unsealed state during electroplating, for example by lowering and lifting the substrate and substrate holder as appropriate to engage and disengage the seal.

The embodiments herein relate to methods and apparatus for electroplating one or more materials onto a substrate. Typically, the embodiments herein utilize a channeled plate positioned near the substrate, creating a cross flow manifold between the channeled plate and substrate, and on the sides by a flow confinement ring. A seal may be provided between the bottom surface of a substrate holder and the top surface of an element below the substrate holder (e.g., the flow confinement ring). During plating, fluid enters the cross flow manifold through channels in the channeled plate, and through a cross flow inlet, then exits at the cross flow exit, positioned opposite the cross flow inlet. The apparatus may switch between a sealed state and an unsealed state during electroplating, for example by lowering and lifting the substrate and substrate holder as appropriate to engage and disengage the seal.

An electroplating apparatus for electroplating metal on a substrate includes a plating chamber configured to contain an electrolyte, a substrate holder configured to hold and rotate the substrate during electroplating, an anode, and an azimuthally asymmetric auxiliary electrode configured to be biased both anodically and cathodically during electroplating. The azimuthally asymmetric auxiliary electrode (which may be, for example, C-shaped), can be used for controlling azimuthal uniformity of metal electrodeposition by donating and diverting ionic current at a selected azimuthal position. In another aspect, an electroplating apparatus for electroplating metal includes a plating chamber configured to contain an electrolyte, a substrate holder configured to hold and rotate the substrate during electroplating, an anode, a shield configured to shield current at the periphery of the substrate; and an azimuthally asymmetric auxiliary anode configured to donate current to the shielded periphery of the substrate at a selected azimuthal position on the substrate.

An electroplating apparatus for electroplating metal on a substrate includes a plating chamber configured to contain an electrolyte, a substrate holder configured to hold and rotate the substrate during electroplating, an anode, and an azimuthally asymmetric auxiliary electrode configured to be biased both anodically and cathodically during electroplating. The azimuthally asymmetric auxiliary electrode (which may be, for example, C-shaped), can be used for controlling azimuthal uniformity of metal electrodeposition by donating and diverting ionic current at a selected azimuthal position. In another aspect, an electroplating apparatus for electroplating metal includes a plating chamber configured to contain an electrolyte, a substrate holder configured to hold and rotate the substrate during electroplating, an anode, a shield configured to shield current at the periphery of the substrate; and an azimuthally asymmetric auxiliary anode configured to donate current to the shielded periphery of the substrate at a selected azimuthal position on the substrate.

An apparatus and method for electrochemically depositing a unitary layer structure using a reactor configured to contain an electrolyte solution with an anode array containing a plurality of independently electrically controllable anodes arranged in a two-dimensional array, a cathode, an addressing circuit for receiving a signal containing anode address data and for outputting a signal causing an anode array pattern; and, a controller. in communication with the addressing circuit and the anode array, configured to electrically control each anode in the anode array to cause an electrochemical reaction at the cathode that deposits a unitary layer structure according to the anode array pattern signal.

An apparatus and method for electrochemically depositing a unitary layer structure using a reactor configured to contain an electrolyte solution with an anode array containing a plurality of independently electrically controllable anodes arranged in a two-dimensional array, a cathode, an addressing circuit for receiving a signal containing anode address data and for outputting a signal causing an anode array pattern; and, a controller. in communication with the addressing circuit and the anode array, configured to electrically control each anode in the anode array to cause an electrochemical reaction at the cathode that deposits a unitary layer structure according to the anode array pattern signal.

A rotational surface treating device with a high treatment efficiency that allows a treatment liquid to be discharged in a short time is provided. When a treatment bath 2 is rotated, parts 20 contact an electrode 50 to be electroplated. In this event, a plating liquid 16 is used as circulated by a pump P. The plating liquid 16 is discharged to the outside through a gap in a side wall 80 for replacement of the plating liquid 16 or the like. During discharge, the plating liquid 16 is not circulated by the pump P. The gap 8 which is formed in the side wall 80 is formed to be smaller than the minimum dimension of the parts 20 on the inner side. The gap 8 is formed to be wider toward the outer side. Thus, water is discharged immediately.