A platform and system for concentration, reduction and regeneration of heavy metals and other contaminants from fluids is provided. The platform has a three-tiered hierarchical porous structure, composed of micropores formed by woven carbon cloth, nanopores formed after carbon nanotube growth on the cloth fibers and mesopores formed by a polymer outer layer. The material of the platform can be incorporated into cells with two electrodes with properly functionalized PDAN grafted 3D carbon as an anode and cathode respectively. Metal ions and toxic anions in water will be captured selectively by primary amine, secondary amine and quaternary amine groups in porous PDAN on the anode. Metals are captured and reduced by the cathode.

Disclosed are a water treatment apparatus including an anode, a cathode disposed to face the anode at a distance therefrom, and at least one electrochemical unit disposed at a distance from the anode and the cathode, respectively, wherein the electrochemical unit includes a layer having bipolarity when a voltage is applied between the anode and the cathode, and a water treatment method using the same.

Self-cleaning electrochemical cells, systems including self-cleaning electrochemical cells, and methods of operating self-cleaning electrochemical cells are disclosed. The self-cleaning electrochemical cell can include a plurality of concentric electrodes disposed in a housing, for example, a cathode and an anode, a fluid channel defined between the concentric electrodes, a separator residing between the concentric electrodes, first and second end caps coupled to respective ends of the housing, and an inlet cone. The separators may be configured to localize the electrodes and dimensioned to minimize a zone of reduced velocity occurring downstream from the separator. The end caps and inlet cone may be dimensioned to maintain fully developed flow and minimize pressure drop across the electrochemical cell.

The present invention is in the field of a system for gas recovery from wastewater, a method for treating wastewater, and a method wherein ammonia and carbon dioxide are recovered. Typically a wastewater stream is fed into the system, treated and stripped from ammonia and carbon dioxide, and a cleaner stream is released.

An electrolytic zinc dosing device that regulates the amount of zinc delivered or dosed into a flowing stream of water as a function, in part, of the current applied to an electrolytic cell and the flow rate of the flowing water. A replaceable electrolytic cell having an anode and a cathode connected to a power supply, and at least one bipolar electrode in aqueous solution between the anode and cathode. Flow rate information and/or total current information are used to determine the dosing quantity of zinc delivered.

An electrolytic cell for treating wastewater comprises an anode assembly, a cathode assembly and at least one bipolar electrode assembly placed between the anode and the cathode assembly such that the anodes of the anode assembly and the cathodes of the cathode assembly are interleaved with the bipolar plates of the bipolar electrode assembly. Each bipolar electrode assembly comprises a series of bipolar electrodes which operate as an anode or as a cathode, stacked in a vertical direction along a threaded bolt made of an electrically conductive material such that the bipolar electrodes operating as anodes are oriented in an opposite direction to the bipolar electrodes operating as cathodes and have their ends overlapping over a predetermined portion and being separated by conductive spacers. In preferred embodiments, only the anodes and the bipolar electrodes operating as anodes are coated with catalyst which saves costs and simplifies the manufacturing process.

An electrolytic cell includes: a cartridge assembly including: a plurality of bipolar electrode plates spaced apart and guide members formed on both sides of the plurality of bipolar electrode plates; a cell body having: a first side; a second side opposite the first side; an opening that extends through the first and second sides to form a housing that receives the cartridge assembly; a first end having an inlet that allows liquid to enter the housing of the cell body and a second end having an outlet that allows liquid to exit the housing of the cell body; a first terminal cap that connects to the first side of the cell body and which has a cathode plate; and a second terminal cap that connects to the second side of the cell body and which has an anode plate.

Self-cleaning electrochemical cells, systems including self-cleaning electrochemical cells, and methods of operating self-cleaning electrochemical cells are disclosed. The self-cleaning electrochemical cell can include a plurality of concentric electrodes disposed in a housing, for example, a cathode and an anode, a fluid channel defined between the concentric electrodes, a separator residing between the concentric electrodes, first and second end caps coupled to respective ends of the housing, and an inlet cone. The separators may be configured to localize the electrodes and dimensioned to minimize a zone of reduced velocity occurring downstream from the separator. The end caps and inlet cone may be dimensioned to maintain fully developed flow and minimize pressure drop across the electrochemical cell.

An electrochlorination system comprises a source of feed fluid, a product fluid outlet, and a plurality of electrochemical cells connected fluidically between the source of feed fluid and the product fluid outlet. The system is configured to operate at least one of the plurality of electrochemical cells at one of a first current density or a first flow rate, and to operate another of the plurality of electrochemical cells at a second current density or second flow rate different from the respective first current density or first flow rate.

An electrochlorination system includes an electrolyzer fluidically connectable between a source of feed fluid and a product fluid outlet, and a sub-system configured to one of increase a pH of the feed fluid, or increase a ratio of monovalent to divalent ions in the feed fluid, upstream of the electrolyzer.