Abstract:
Systems and methods for controlling mixing between one or more fluids are provided. The systems and methods may utilize a vessel comprising one or more zones product where the zones are configured to minimize mixing between one or more fluids. Certain systems and methods may utilize a vessel comprising a tortuous flow path. Other systems and methods may utilize a vessel comprising one or more zones.
Abstract:
Systems and methods for treating water are provided. The systems and methods may utilize an electrochemical water treatment device comprising ion exchange membranes. In certain systems and methods, a concentrate stream and a dilution stream may be in fluid communication with ion exchange membranes. The ion exchange membranes may be configured to provide a ratio of a pH of the concentrate stream and a pH of the dilution stream to be less than about 1.0. In some instances, the LSI of the concentrate stream may be less than or about 1.0. In certain instances, the electrochemical water treatment device does not require a reverse polarity cycle.
Abstract:
Systems and methods for controlling mixing between one or more fluids are provided. The systems and methods may utilize a vessel comprising one or more zones where the zones are configured to minimize mixing between one or more fluids. Certain systems and methods may utilize a vessel comprising a tortuous flow path. Other systems and methods may utilize a vessel comprising one or more zones.
Abstract:
Systems and methods for treating water are provided. In certain examples, the water to be treated is seawater. The systems and methods may utilize an electrochemical water treatment device comprising ion exchange membranes. In at least one example, the electrochemical water treatment device may be configured to perform a desalination process on seawater. In some examples, the ion exchange membranes may be configured to provide a ratio of a pH of the concentrate stream and a pH of the dilution stream to be in a range of from about 0.9 to about 1.2.
Abstract:
Systems and methods for treating water are provided. The systems and methods may utilize an electrochemical water treatment device comprising ion exchange membranes. In certain systems and methods, a concentrate stream and a dilution stream may be in fluid communication with ion exchange membranes. The ion exchange membranes may be configured to provide a ratio of a pH of the concentrate stream and a pH of the dilution stream to be less than about 1.0. In some instances, the LSI of the concentrate stream may be less than or about 1.0. In certain instances, the electrochemical water treatment device does not require a reverse polarity cycle.
Abstract:
Systems and methods for treating water are provided. The systems and methods may utilize an electrochemical water treatment device comprising ion exchange membranes. In certain systems and methods, a concentrate stream and a dilution stream may be in fluid communication with ion exchange membranes. The ion exchange membranes may be configured to provide a ratio of a pH of the concentrate stream and a pH of the dilution stream to be less than about 1.0. In some instances, the LSI of the concentrate stream may be less than or about 1.0. In certain instances, the electrochemical water treatment device does not require a reverse polarity cycle.
Abstract:
Systems and methods for treating water are provided. The systems and methods may utilize an electrochemical water treatment device comprising ion exchange membranes. In certain systems and methods, a concentrate stream and a dilution stream may be in fluid communication with ion exchange membranes. The ion exchange membranes may be configured to provide a ratio of a pH of the concentrate stream and a pH of the dilution stream to be less than about 1.0. In some instances, the LSI of the concentrate stream may be less than or about 1.0. In certain instances, the electrochemical water treatment device does not require a reverse polarity cycle.