Proposed are a manufacturing method of a composite capacitive desalination electrode which can increase the desalination efficiency and as a new structure with more excellent mechanical and chemical resistance, and a composite capacitive desalination electrode and assembly. The manufacturing method includes the following steps: a) forming a composite microporous membrane by forming an ion exchange resin layer on a surface of the microporous membrane; and b) forming the composite microporous membrane prepared in the step a) on both sides of an electrode sheet, thereby producing a first unit including the composite microporous membrane and the electrode sheet. The steps are performed in a single process line by an in-line continuous process.

The present invention relates to methods for selective separation of ionic species from an ionic solution based on said species' ionic hydrated size, the method comprising, inter alia, passing an ionic solution comprising ions having distinct hydrated sizes, through an electrode capacitor assembly comprising at least one carbon-based electrode which is modified with negatively or positively charged surface groups. Further provided is a method for selective separation of ionic species from an ionic solution comprising passing the ionic solution comprising a first positively charged ion and a second positively charged in through an electrode capacitor assembly, wherein the first modified electrode comprises carbon modified with sulfonate surface groups.

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.

A method for selective adsorption of lead ions from heavy metal wastewater by electric field enhancement relating to a method for recovering lead ions from heavy metal wastewater. The method aims to solve the technical problems that it is difficult to recover heavy metals from a complex water environment in well-targeted manner and recovery purity is poor because of poor selectivity of the existing adsorbents. The adsorption selectivity to Pb.sup.2+ is enhanced under an electric field by applying a tannic acid@graphene oxide conductive aerogel material to water heavy metal electrochemical adsorption system as a conductive adsorbent. In the method, the conductive layer of the tannic acid@graphene oxide conductive aerogel material may be optimized through electrochemical reduction, so that the material has better conductivity, and has better selectivity to lead ions under an electric field.

An electrocoagulation unit that may include an outer shell, and a set of electrodes disposed therein. At least two electrodes are separated from an adjacent electrode by an electrode gap. The outer shell may further include a fluid inlet; a fluid outlet; a first busbar opening with a first busbar gland associated therewith.

Provided is a method of forming a filter module. The method includes: forming a non-pore ion-exchange membrane including: preparing a mixed solution of a polymer material and an ion-exchange material; and electrospraying the mixed solution to obtain the non-pore ion-exchange membrane; and interposing the non-pore ion-exchange membrane between a first polymer nanofiber web and a second polymer nanofiber web to form the filter module.

A deep sludge dewatering method using electroosmosis with filter bags, including (1) placing a filter bag on a slope on which a cathode electrode is arranged; (2) injecting sludge into the filter bag, and after the filter bag is filled with the sludge, closing an inlet of the filter bag; and (3) laying an anode electrode on the filter bag filled with the sludge, and connecting the cathode electrode and the anode electrode to a DC power supply via an electric wire, and carrying out energization for electroosmosis so that water flows down the slope. The present invention can be used for recycling of the sludge produced in underground and tunnel excavation projects, and has the advantages of large processing capacity, simple process, good treatment effect and available resource recycling.

The present invention is directed to a porous electrode that includes a porous substrate and a coating. The porous substrate includes internal pores having internal pore surfaces. The coating covers at least a portion of the interior pore surfaces and is electrically conductive and ion-binding. The present is also directed to methods of using the porous electrode of the present invention in a variety of applications (e.g., water desalination and/or capacitive deionization) where an ion from a liquid electrolyte is bound to the substrate and/or released during electrochemical operation. The present invention is also directed to a capacitive deionization system for deionizing water that includes a compressible porous electrode of the present invention.

A reactor system for reacting liquid phase chemical species in a liquid includes a reactor vessel for containing the liquid phase and a gas phase. The reactor vessel can have a gas injection port, a gas exit port, and a liquid-gas interface location within the reactor vessel. A pulsed discharge cathode and anode are provided for creating a pulsed discharge electric field at the liquid-gas interface location. A pulsed discharge power supply delivers a pulsed power input to the pulsed discharge cathode and anode, and thereby creates a plasma comprising ions at the liquid-gas interface location. A secondary electric field source is provided for directing a secondary electric field transverse to the liquid-gas interface. The secondary electric field will drive some of the ions from the gas phase into the liquid phase to react with the liquid phase chemical species. A method for reacting a liquid phase chemical species is also disclosed.

A desalination battery includes a working intercalation electrode in a first compartment, a counter intercalation electrode in a second compartment, both compartments including saline water solution with an elevated concentration of dissolved salts, an ion exchange membrane arranged between the compartments, a voltage source arranged to supply voltage to the electrodes, and a sacrificial compound configured to neutralize charge within the first compartment at a predetermined voltage while being consumed by oxidation or reduction reactions upon an activation of the working electrode.