A capacitive deionization desalination device is provided. The capacitive deionization desalination device includes a mesh spacer and two carbon nanotube composite electrodes. The mesh spacer is located between the two carbon nanotube composite electrodes. Each carbon nanotube composite electrode includes at least one carbon nanotube film structure and a composite carbon layer, and the carbon nanotube film structure includes at least two carbon nanotube films, and the composite carbon layer includes activated carbon and carbon black, and the composite carbon layer is located on the carbon nanotube film structure.

An apparatus and method are provided for enhanced capacitive deionization of contaminated water. The apparatus includes a contaminated water source, a capacitive deionization reactor and a flushing fluid source that is used to flush concentrated contaminants from the capacitive deionization reactor while that reactor is isolated from the contaminated water source.

The disclosure refers to a method, reaction chamber and system for treatment of liquids in continuous flow including the steps of receiving a liquid for treatment in a reaction chamber; converting q flow of liquid for treatment in a biphasic liquid-gas flow; directing the biphasic flow to a central section of the reaction chamber, where an electric field is applied; ionizing the gaseous fraction of the biphasic flow that passes through said central section sustaining an ionization regime generating non-thermal plasma throughout the central section of the reaction chamber leading the biphasic flow under the ionization regime to a discharge section of the reaction chamber, where the electric field is applied, generating the deionization of the gaseous fraction and causing the biphasic flow to reduce its velocity, which results in the condensation of biphasic flow; and removing a flow of treated liquid from said discharge section.

The present invention provides return flow ICP and ED systems and methods that can be used for water desalination and/or concentration of a wide range of target brine and other aqueous and contaminated streams.

A method for reacting a liquid phase chemical species includes the steps of providing liquid phase containing at least one liquid phase chemical species, providing a gas phase, and providing a reactor vessel for containing the liquid phase and the gas phase. The liquid phase and the gas phase are placed in the reactor vessel so as to form a liquid-gas interface between the liquid phase and the gas phase within the reactor vessel. A pulsed discharge cathode and anode are provided for creating a pulsed discharge electric field at the liquid-gas interface. A pulsed power input to the pulsed discharge cathode and anode is provided, thereby creating a plasma comprising ions at the liquid-gas interface. A secondary electric field is directed transverse to the liquid-gas interface, wherein the secondary electric field will drive ions from the gas phase into the liquid phase to react with the liquid phase species.

Disclosed are a deionization electrode having ion adsorption layers and ion selective membranes formed at opposite ends thereof, an electrode module configured such that deionization electrodes are stacked, and a deionization unit having electrode modules received therein to separate ions from water. The deionization electrode includes a current collector configured to have a circular flat structure, the current collector having a first hole formed therein, a first porous adsorption layer located on one surface of the current collector, the first adsorption layer being configured to have a flat structure, a second porous adsorption layer located on the other surface of the current collector, the second adsorption layer being configured to have a flat structure, a first ion selective membrane located on the surface of the first adsorption layer, and a second ion selective membrane located on the surface of the second adsorption layer.

An organic compound destruction apparatus and method are provided. In another aspect, a laterally oriented discharge arc generated from an electrode in a reactor, destroys an undesired or contaminant organic molecule in a liquid solution. Another aspect includes a system which uses electrodes and a magnetic field to generate and drive laterally oriented discharge arcs in a reactor to destroy organic compounds, such as PFAS molecules, in a liquid. Another aspect includes using at least one pair of co-axial electrodes submerged in a liquid to concentrate organic contaminants around the center electrode where gas bubbles are generated to capture and transport the contaminants to the plasma region above the liquid surface. Still another aspect includes a system which uses a grid or mesh electrode to create a discharge arc in a plasma chamber to destroy organic compounds, such as PFAS molecules, in a liquid.

A capacitive deionization desalination device is provided. The capacitive deionization desalination device includes a mesh spacer and two carbon nanotube composite electrodes. The mesh spacer is located between the two carbon nanotube composite electrodes. Each carbon nanotube composite electrode includes at least one carbon nanotube film structure and a composite carbon layer, and the carbon nanotube film structure includes at least two carbon nanotube films, and the composite carbon layer includes activated carbon and carbon black, and the composite carbon layer is located on the carbon nanotube film structure.

An apparatus is provided for treating a liquid with a plasma. The apparatus includes one or two dielectric barriers, and the dielectric barrier(s) and high voltage electrode define a discharge zone therebetween. A high voltage electrode may be electrically insulated from the discharge zone by the inner dielectric barrier. In this apparatus, the outer dielectric barrier is gas and the discharge zone is configured to accept a gas flow therethrough.

Tandem electrodialysis (ED) cell systems and methods for using the tandem ED cell systems to extract and recover ions from ion-containing solutions are provided. The tandem ED cell systems are composed of ion-extraction and ion-recovery ED cells. A redox couple contained in the anolyte of the ion-extraction ED cell is different from a redox couple contained in the catholyte of the ion-extraction ED cell. The electrode reactions in the ion-extraction ED cell are reversed in the ion-recovery ED cell, with the anolyte and catholyte of the two ED cells swapped and continuously circulated. As a result, the redox species in the anolyte and catholyte of the two cells are never depleted, which allows for achieving ion extraction and ion recovery with the use of a minimal amount of the redox couples.