An electrolyzed water generation device is provided with a first flow passage delivering electrolyzed water generated in one of a first polar chamber and a second polar chamber of an electrolytic chamber, a second flow passage delivering electrolyzed water generated in the other one of the first polar chamber and the second polar chamber, a double autochange crossline valve in which a flow rate regulating valve 74 and a flow passage switching valve 85 are interlocked, a polarity switching unit 51 switching the polarities of a first power feeder 41 and a second power feeder 42, and a determination unit 52 determining switching timing of the polarity switching unit 51 and the flow passage switching valve 85. The determination unit 52 integrates electrolysis time in the electrolytic chamber 40 and determines that the switching timing arrives when an integrated electrolysis time t reaches a predetermined threshold value T without the polarity being switched.

A method of operating an electrochemical device includes periodically discharging a volume of concentrate reject in a timed batch cycle and replacing the concentrate reject with feed water. An electrochemical water treatment system includes a recycle line having a valve controlled by a control module. The control module periodically opens the valve to discharge concentrate reject from the recycle line in a batch timed cycle. The recycle line is fed with feed water to replace the discharged concentrate reject.

The present disclosure relates to a biocide-generating device for outputting a biocide to a water system. The biocide-generating device includes a housing having a water inlet for receiving water from the water system and a water outlet for outputting water containing biocide to the water system. The biocide-generating device also includes an electrode arrangement having first and second electrodes positioned in the housing for generating biocide in the water within the housing, and an electrical power circuit for establishing a flow of electrical current between first and second electrodes of the electrode arrangement for generating the biocide in the water within the first chamber electrolytic cell. Features for enhancing heat transfer, sealing and electrical isolation are incorporated into the biocide-generating device.

The present disclosure describes systems and methods for wastewater treatment. In some embodiments, a system may include one or more of a pair of electrodes, a first membrane selectively permeable to a first wastewater nutrient, a second membrane selectively permeable to a second wastewater nutrient, and at least one spacing frame comprising a structural element, a gasket, and a flow channel. In some embodiments, the system may further include a septic tank.

The present disclosure relates to a biocide generating system for inhibiting bio-fouling within a water system of a watercraft. The water system is configured to draw water from a body of water on which the watercraft is supported. The biocide generating system includes an electrode arrangement adapted to be incorporated as part of an electrolytic cell through which the water of the water system flows.

The present invention provides a system and method for treatment of wastewater from industry, particularly water contaminated with pesticides, herbicides, and other contaminants. The system improves efficiency of contaminant removal from waste waters, reducing the volume and mass of the extracted waste and increasing the yield of usable water. Particularly, the system and method of the present invention provides improved electrocoagulation systems and techniques.

An electrode apparatus for removing contaminants from a fluid is provided. In another aspect, an electrochemical destruction apparatus for wastewater effluent using Boron-doped diamond electrodes is employed. A further aspect of the present apparatus includes a fluid-carrying conduit, electrodes located within the conduit, an electrical controller connected to the electrodes, a sensor connected to the controller being adapted to sense a chemical characteristic associated with contaminants in the fluid, and the controller automatically varying an electrical characteristic associated with at least one of the electrodes based, at least in part, on an input from the sensor. Yet another aspect includes a programmable controller and software which automatically employ a feedback control loop to increase or decrease electrical current density to contaminant-removing electrodes.

An apparatus for oxygenating water includes a discharge chamber with a fluid inlet and a fluid outlet, an electronic unit coupled to the discharge chamber, and a power source configured to power the electronic unit. The electronic unit is configured to interact with water disposed within the discharge chamber. The electronic unit is configured to apply a sequence of increasing pulses to the water to produce oxygenated water.

Provided is an UFB generating apparatus and an UFB generating method capable of efficiently generating an UFB-containing liquid with high purity. To this end, the ultrafine bubble generating apparatus includes a pre-processing unit that performs predetermined pre-processing on a liquid W and a generating unit that generates ultrafine bubbles in the liquid on which the pre-processing is performed. The generating unit generates the ultrafine bubbles by causing a heating element, which is provided in the liquid on which the pre-processing is performed, to generate heat to generate film boiling on an interface between the liquid and the heating element.

An electrolyzed water generation device is provided with a first flow passage delivering electrolyzed water generated in one of first polar chamber and second polar chamber of an electrolytic chamber, a second flow passage delivering electrolyzed water generated in the other one of the first polar chamber and second polar chamber, a double autochange crossline valve in which a flow rate regulating valve 74 and a flow passage switching valve 85 are interlocked, a polarity switching unit 51 switching the polarities of a first power feeder 41 and a second power feeder 42, and a determination unit 52 determining the switching timing of the polarity switching unit 51 and the flow passage switching valve 85. The determination unit 52 determines that the switching timing arrives when a predetermined time passes without detecting water supply to the electrolytic chamber after electrolysis is performed by a predetermined number of times or more in the electrolytic chamber without the polarities being switched.