Abstract: Method and plant for continuous chrome plating of metal bars, tubular elements and similar, wherein the bar to be chromed is made move forward fastly in a device of chrome plating without of tank of chrome plating including a plurality of anodic cells of chrome plating with tubular-torx shape, into which an electrolytic solution flows with high density of current, for forming on the bar a multi-layer chromium plating while the bar moves forward through the anodes-cells themselves, and wherein the device is characterized in feeding the electrolytic solution with a flow axially distributed and with a circulation of the electrolyte in a turbulent flow, controlled through the anode of chrome plating, said plant including furthermore many cooling stations of the bar by a jet of liquid with cryoscopic thermal step, the sealing of the bath is guaranteed by gaskets in plastic material which are reinforced by armonic steel springs.

Abstract: Provided is a method and an apparatus for producing hydrogen from salt water by electrolysis. The apparatus includes at least one pair of electrodes, wherein the pair of electrodes comprises a first zinc plated electrode and a second zinc plated electrode spaced apart from the first zinc plated electrode, a controller for supplying direct electrical current across the first and second electrodes such that the first and second electrodes are oppositely charged, and a tank containing an electrolytic solution including salt water and a mild acid. The first and second electrodes are immersed in the electrolytic solution.

Abstract: Electrodeposition painting systems may include an electrodeposition bath containing an electrodeposition paint solution, wherein the electrodeposition paint solution is in contact with an electrodeposition bath anode that charges the paint such that it electrocoats parts submerged therein to form electrocoated parts, a rinse tank that rinses the electrocoated parts, wherein a rinse tank reservoir of the rinse tank is capable of fluid communication with the electrodeposition bath, a filter that filters the electrodeposition paint solution to separate filtered water from the paint, and an ionizer assembly including one or more electrodes in contact with the filtered water and a power supply connected to the one or more electrodes, wherein the power supply causes a plurality of electrode ions from the one or more electrodes to enter the filtered water to produce filtered water including electrode ions such that the filtered water including electrode ions flows into and sterilizes the electrodeposition paint solu

Abstract: Disclosed is a method of recovering metal from waste plating stream and using the recovered metal comprising: providing a waste metal plating stream containing metal ions in an aqueous solution; passing the waste metal plating stream containing the metal ions into an electrochemical cell assembly having an inlet for the waste metal plating stream, a plurality of alternating anodes and cathodes porous to the waste metal solution and an exit from the cell; passing the waste metal plating stream through pores of the cathode; passing an electrical current through the anodes and cathodes, thereby depositing a portion of the metal ions onto the cathodes and reducing the amount of the metal ion in the solution from that in the introduced waste metal plating stream; recovering the deposited metal from the cathode; and using the recovered deposited metal as a source of soluble metallic anode to be deposited on to a substrate in a subsequent metal plating process.

Abstract: An insulating end cap for a cylindrical electrolysis cell the type comprising at least two tubular electrodes with a cylindrical membrane arranged co-axially between them, comprises a first annular section with first and second axial ends, having at its first axial end a circular seating or one end of an outer cylindrical electrode and at its second end a circular aperture, of smaller diameter than the circular seating and co-axial therewith, to accommodate one end of the membrane. A second annular section of the end cap is detachably secured to the first and has a central circular aperture of smaller diameter than the central aperture of the first section and co-axial therewith, to accommodate one end of the inner cylindrical electrode. The two part construction of the end cap facilitates the assembly of the cell, and reduces the likelihood of breakage of the fragile ceramic membrane.

Abstract: A method and apparatus for cleaning a wafer with a metal exposed through an insulator, through the use of a wet cleaning tank in concert with a feedback system on the potential difference between two leads of the wet cleaning tank. The cleaning tank has a bath in which the wafer and the two leads are immersed. The potential difference between the two leads is regulated when the feedback system detects a change in the potential across the two leads.

Abstract: An enhanced gradient dragout system conserves plating chemicals, including precious metals by providing a series of tanks with cascading rinse solutions having a flow rate controlled by heating the first tank to increase the evaporation rate. A portion of the concentrated solution in the heated tank is returned to the process tank. The system minimizes the requirements for clean rinse water, and the need for emptying contaminated rinse tanks with associated recovery and disposal environmental and cost issues. The low cost system is flexible and the process is adapted to the material and process requirements of the plating line.

Abstract: An enhanced gradient dragout system conserves plating chemicals, including precious metals by providing a series of tanks with cascading rinse solutions having a flow rate controlled by heating the first tank to increase the evaporation rate. A portion of the concentrated solution in the heated tank is returned to the process tank. The system minimizes the requirements for clean rinse water, and the need for emptying contaminated rinse tanks with associated recovery and disposal environmental and cost issues. The low cost system is flexible and the process is adapted to the material and process requirements of the plating line.

Abstract: Method and apparatus for handling water used in plating processes to eliminate discharge of pollutants including a plating tank for chrome plating selected materials, at least one rinse tank which holds rinse water where parts from the plating tank are rinsed to remove chrome compounds used in the plating tank and transfer means to transfer water from the rinse tank to a purification tank where hydrazine is added to the rinse water in quantities sufficient to maintain selected pH in the water returned to one of the rinse tanks for precipitation of the chromic compounds to chromic hydroxide which can be easily filtered for disposal as a dry material. High quality water such as deionized water is added to the rinse tank to makeup lost water and a catalyst such as cobalt salt can be added to the purification tank to assist in reduction of the chromic compounds.

Abstract: The invention describes a process for the electrolytical coating of an object of steel on one or both sides. Preferably, the object is a steel strip with zinc or a zinc iron alloy. Zinc or a zinc iron alloy is deposited on the object when the object is connected to form the cathode of a galvanic cell in an aqueous solution of zinc chloride and iron chloride with a pH of 0.1 to 3.0. The zinc chloride solution has a concentration of 50 to 1000 g/l for the deposition of metallic zinc. A partial flow of electrolyte solution is past continuously into a column filled with metallic zinc, where the trivalent iron formed there during the electrolysis is reduced to a bivalent iron, and metallic zinc is dissolved simultaneously therewith. The invention also describes an apparatus for the electrolytical coating of an object of steel.

Abstract: This is to a process for chromium plating metal articles spray rinsing the metal article after it has been cleaned, acid treated, nickel plated, and chromium plated over rinse tanks which are empty except for the rinse collected therein. The rinse water is recirculated to the respective treating tanks as needed.

Abstract: In a retardation installation having a container holding the adsorber material capable of accepting acid, in particular adsorber resin, and a feed for a watery acid-salt-solution, for example from an anodizing bath, a further feed for a regenerating solution to regenerate the adsorber material, in particular demineralized Water in opposite flow to the acid-salt-solution, as well as a drain for the treated acid-salt-solution which has passed the adsorber material and with at least one pump for the transport of the acid salt solution and/or the regenerating solution, precisely one pump is provided for which is configured as a compressed air-diaphragm pump and which exhibits a device for stroke counting as well as a device for the control of the volume flow of acid-salt-solution or regenerating solution on the a basis of the stroke count of the compressed air-diaphragm pump.

Abstract: The total organic content (TOC) of an aqueous composition is reduced to 200 ppm or less by subjecting the composition to electrolysis whereby the pH of the composition at the start of the electrolysis is about 1.8 to about 7 to thereby electrolytically decompose organic materials contained in the aqueous composition.

Abstract: The present invention relates to a method of completely recovering nickel and zinc metal from multiple plating process waste streams by first separating the waste streams into a clean, relatively constant flow and/or concentration fraction and a dirty, variable flow and/or concentration fraction. Metal is recovered from the clean fraction by ion-exchange so as to concentrate the extracted metals for direct return to the plating bath. The effluent from the ion-exchange step is then blended with the dirty, variable flow and concentration fraction. This blended flow is first neutralized and then precipitated in a two-stage process using a sodium hydroxide solution. The resultant slurry containing the metal precipitate is filtered to yield a filter cake containing recovered nickel and zinc. This filter cake can then be further processed to recover the metal for reintroduction into the plating bath or for other uses.