An apparatus for removing contaminants from fluid is disclosed. The apparatus includes a rotating electrode assembly including an inner shaft rotatably mounted within the housing and a first rotatable planar electrode extending radially outward from the inner shaft. The apparatus also includes a first planar stationary electrode having a first opening, the first opening shaped to permit the inner shaft to pass through the first opening, the first planar stationary electrode extending parallel to the first rotatable planar electrode, wherein the first planar stationary electrode and the first rotatable planar electrode are configured to be coupled to an external source. In addition, the apparatus includes a motor assembly including a motor and a first outer shaft coupled to the inner shaft. The rotating electrode assembly is configured to be removed from the housing when the inner shaft is decoupled from the first outer shaft.

Various embodiments relate to methods and systems for removing phosphorus and/or nitrogen from water. A method of removing phosphorus and nitrogen from water includes passing starting material water including nitrogen and phosphorus through an elevated pH phosphorus removal stage. The method includes passing the water through an electrolytic nitrogen removal stage. The method includes passing the water through a galvanic phosphorus removal stage. The water produced by the method has a lower phosphorus concentration and a lower nitrogen concentration than the starting material water.

An electro-separation apparatus for separation of drilling fluids is provided. The apparatus can include a reaction chamber and a set of electrode plates provided in the reaction chamber. A sediment outlet can be provided near a bottom of the reaction chamber and wiper blades can be provided for sweeping sediment that has collected on the electrode plates towards the sediment outlet.

An electrocoagulation (EC) unit that performs an electrocoagulation process on wastewater or the like. In one embodiment, the EC unit includes a reaction tank formed from a non-conductive material, charge plates within the reaction tank that are spaced at a distance, intermediate plates disposed within the reaction tank between the charge plates, and plate conductors configured to electrically couple the charge plates to a power source. The bottom of the reaction tank tapers toward one or more ports which act as an ingress and egress point for the EC unit.

This disclosure provides techniques for treatment of aqueous matrices using electrolysis to produce soluble metals. An aqueous matrix of interest is passed through an electrolysis device with at least one consumable electrode, which dissolves under applied current, transferring a desired reagent to the aqueous matrix of interest. In one embodiment, the electrolysis device is used in a water delivery network to passivate hexavalent chromium (Cr6) and/or convert it to trivalent chromium; the electrode can be made of food-grade metal tin, which is electrolyzed to form a stannous reagent, which then reacts with the Cr6. The disclosed techniques provide for Cr6 passivation without requiring the use of concentrated acids or other harmful substances. Long term reagent generation efficiency can be enhanced through the use of cleaning processes which maintain a fresh electrode surface in contact with the aqueous matrix of interest.

Method and apparatus for a low maintenance, high reliability on-site electrolytic generator incorporating automatic cell monitoring for contaminant film buildup, as well as automatically removing or cleaning the contaminant film. This method and apparatus preferably does not require human intervention to clean. For high current density cells, cleaning is preferably performed by reversing the polarity of the electrodes and applying a lower current density to the electrodes, preferably by adjusting the salinity or brine concentration of the electrolyte while keeping the voltage constant. Electrolyte flow preferably comprises water and brine flows which are preferably separately monitored and automatically adjusted. For bipolar cells, flow between modules arranged in parallel is preferably approximately equally distributed between modules and between intermediate electrodes within each module.

A method for purification of water with a water purifier. The water purifier includes an anode and a cathode as electrodes in such a way that a gap remains between the anode and the cathode. In the method, an electric field is generated between the anode and the cathode, water for purification is conveyed to the gap and an additive enhancing floc formation is introduced to water for purification or to purified water in an amount of less than 50 g and at least 1 g, measured as dry matter, per each cubic metre of water for purification. Floc material manufactured with the method, when water for purification is municipal wastewater. The use of the floc material produced in this way as a soil conditioner or for manufacturing a soil conditioner.

An automated waste water treatment system includes a collection tank constructed to hold waste water, a first flow line connected to the collection tank to output the waste water from the collection tank, an electrocoagulation unit that receives the waste water and outputs the waste water as coagulated waste water to a flow line, a polymer dosage tank to provide a polymer dosage into the flow line where the polymer dosage mixes with the coagulated waste water to produce and output flocculated waste water. A clarifier connected to the flow line receives the flocculated waste water and produces sludge-free waste water and concentrated sludge, a series of filters to output filter-treated water, and an ultrafiltration system that receives filter-treated water and outputs ultrafiltration-treated water to a reverse osmosis system.

An efficient electrochemical pre-scaling water treatment device is disclosed. The device comprises an enclosed box, wherein anode positioning connecting shafts, anode plates, cathode plates and scrapers are distributed in a length direction of the closed box, the scrapers are fixed to a scraper holder, the anode plates are fixed to the anode positioning connecting shafts, and the cathode plates are fixed to a central shaft; the anode positioning connecting shafts, the scraper holder and the central shaft are fixed on the enclosed box; in the width direction of the enclosed box, a water inlet is provided at a first side of the enclosed box, a water outlet and a sewage outlet are provided at a second side of the enclosed box, and exhaust holes are provided at a top of the enclosed box.

Various embodiments relate to an electrochemical cell for removal of materials from water and methods of using the same. A method of removing phosphorus from water includes immersing an electrochemical cell in water including phosphorus to form treated water including a salt that includes the phosphorus. The electrochemical cell includes an anode including Mg, Al, Fe, Zn, or a combination thereof, a cathode including Cu, Ni, Fe, or a combination thereof. The method includes separating the salt including the phosphorus from the treated water, to form separated water having a lower phosphorus concentration than the water including phosphorus.