Provided are a capacitive deionization electrode and a method of manufacturing the same, which have an effect of providing a capacitive deionization electrode at a low cost as compared with the conventional technology while having a high level of deionization performance and durability.

The present disclosure provides an electrode material and a method for preparing the same. The electrode material includes 3 to 7 wt % of a graphene material, 4 to 8 wt % of a photocatalytic nano-material, 3 to 9 wt % of a binder system, and a balance of a glass fiber cloth, based on a total weight of the electrode material. The method includes providing a graphene-based precursor solution;

agitating and dispersing a glass fiber cloth to obtain an uniform slurry; wet forming the slurry to obtain a glass fiber sheet, and cleaning and drying the glass fiber sheet; putting the glass fiber sheet into the graphene-based precursor solution for in-situ synthesis to obtain a glass fiber paper; and immersing the glass fiber paper with a binder system and drying the glass fiber paper to obtain the electrode material.

Systems and processes for purifying and concentrating a liquid feed stream are disclosed. In the systems, the concentrated liquid output from the high pressure side of a reverse osmosis stage is used as the draw solution in the low pressure side of the reverse osmosis stage in a configuration called osmotically assisted reverse osmosis. This reduces the osmotic pressure differential across the membrane, permitting high solute concentrations to be obtained, hastening the purification of the liquid. Reduced system pressures are also obtained by arranging multiple osmotically assisted reverse osmosis stages in a cross-current arrangement. Overall system energy consumption is reduced compared to conventional thermal processes for high concentration streams.

Electrochemical water treatment devices are disclosed. The device includes a feed inlet fluidly connectable to a source of water including dissolved silica and a chlorine-containing compound and an electrochemical separation module fluidly connectable to the feed inlet. The electrochemical separation module includes a dilution compartment, a concentration compartment, an ion exchange membrane positioned between the dilution and concentration compartment, and first and second electrodes. A first portion of a volume of the dilution compartment includes a first ion exchange media positioned proximate to the feed inlet. A second portion of the volume of the dilution compartment includes a second ion exchange media positioned distal to the feed inlet. The first ion exchange media has a greater resistance to the chlorine-containing compound than the second ion exchange media. Methods of reducing a concentration of dissolved silica in water are disclosed. Methods of facilitating treatment of water containing dissolved silica are disclosed.

Provided are apparatus and method for controlling total dissolved solids, and water treatment apparatus including apparatus for controlling total dissolved solids. The total dissolved solid controlling apparatus includes, a filtering unit including a deionizing filter removing dissolved solids from inflow raw water by an input current and, a control unit controlling the input current such that water discharged from the deionizing filter corresponds to target total dissolved solids.

A deionization battery cell including a first electrode compartment containing a first intercalation host electrode and includes a first water stream compartment in fluid communication with the first electrode compartment. The deionization battery cell further includes a second electrode compartment containing a second intercalation host electrode and a second water stream compartment in fluid communication with the second electrode compartment. The deionization battery cell also includes an ion exchange membrane assembly including a plurality of anion exchange membranes separated from each other, and from one or more cation exchange membranes positioned between the anion exchange membranes, by a plurality of intervening water stream compartments. The first and second water stream compartments are separated from one another by the ion exchange membrane assembly.

A flow-electrode cartridge unit and a submerged flow-electrode capacitive deionization device using the same are proposed. The flow-electrode cartridge unit includes a pair of porous current collector plates arranged to face each other in a spaced apart state from each other in a first direction, a pair of ion separation membranes positioned on respective outer surfaces of the porous current collector plates in the first direction, a channel frame for wrapping around the pair of porous current collector plates and the pair of ion separation membranes to expose each of the ion separation membranes in the first direction, thereby forming a flow electrode channel between the pair of porous current collector plates, a pair of communication holes formed in the channel frame and communicating the flow electrode channel to an outside, and an electrode terminal formed in the channel frame and electrically connected to the porous current collector plates.

A fluid treatment apparatus and related methods involving the use of replaceable treatment cartridges that include a treatment media, wherein the treatment cartridge is electrically enhanced to form regions of differing polarity within the cartridge. The treatment cartridge can include a pair of fixed polarity conductors that can be electrically connected to a power source so as to induce regions of differing polarity within the cartridge. The fluid treatment apparatus can be utilized to treat liquids including aqueous solutions as well as gases such as an air supply by exposing the fluid to the regions of differing polarity.

A method for treating wastewater having one or more of suspended solids, dissolved solids, biological oxygen demand includes solids filtration followed by a bi-polar/bi-directional flow through ionic module fitted with anionically/cationically charged plates followed by a sub-sonic resonance module followed by another bi-polar/bi-directional flow through ionic module followed by a ultra-sonic resonance module followed by one or more anion/cation collection membrane modules. Recycle is provided in each step, wherein each step may be repeated, and wherein one or more of the steps can be bypassed.

Systems and processes for purifying and concentrating a liquid feed stream are disclosed. In the systems, the concentrated liquid output from the high pressure side of a reverse osmosis stage is used as the draw solution in the low pressure side of the reverse osmosis stage in a configuration called osmotically assisted reverse osmosis. This reduces the osmotic pressure differential across the membrane, permitting high solute concentrations to be obtained, hastening the purification of the liquid. Reduced system pressures are also obtained by arranging multiple osmotically assisted reverse osmosis stages in a cross-current arrangement. Overall system energy consumption is reduced compared to conventional thermal processes for high concentration streams.