Abstract: A liquid desiccant regenerator configured to produce a first output stream with a higher concentration of a liquid desiccant than a first input stream. The regenerator also produces a second output stream with a lower concentration of the liquid desiccant than a second input stream. Regeneration of the liquid desiccant in the liquid desiccant regenerator decreases a temperature of the liquid desiccant regenerator. The system includes an air contactor coupled to the first output stream and exposing an input air stream to the first output stream. The first output stream absorbs water from the input air stream to form at least one diluted output desiccant stream. A heat pump of the system is thermally coupled to move the heat from the first output stream to the liquid desiccant regenerator. The heat moved to the liquid desiccant regenerator increases an efficiency of the liquid desiccant regenerator.

Abstract: A liquid desiccant regenerator configured to produce a first output stream with a higher concentration of a liquid desiccant than a first input stream. The regenerator also produces a second output stream with a lower concentration of the liquid desiccant than a second input stream. Regeneration of the liquid desiccant in the liquid desiccant regenerator decreases a temperature of the liquid desiccant regenerator. The system includes an air contactor coupled to the first output stream and exposing an input air stream to the first output stream. The first output stream absorbs water from the input air stream to form at least one diluted output desiccant stream. A heat pump of the system is thermally coupled to move the heat from the first output stream to the liquid desiccant regenerator. The heat moved to the liquid desiccant regenerator increases an efficiency of the liquid desiccant regenerator.

Abstract: The present disclosure is directed to an electrodialytic stack with a concentrate stream that moves through a concentrate flow path bounded by a central ion exchange membrane and a first outer ion exchange membrane. A dilute stream moves through a dilute flow path bounded by the central ion exchange membrane and a second outer ion exchange membrane. A redox shuttle loop is separated from the concentrate and dilute streams by the first and second outer ion exchange membranes, respectively. The outer ion exchange membranes are a different type than the central ion exchange membrane. Electrodes are operable to apply a voltage across the stack. At least one collection of ion exchange materials is located in at least one of the flow paths. The ion exchange materials migrate ions between the central ion exchange membrane and at least one of the outer ion exchange membranes.

Abstract: An electrochemical compression system utilizes a preheater to heat an electrochemically active working fluid to a superheated temperature delta prior compression. Heating the electrochemically active working fluid to a superheated temperature ensures there will be no condensation before the fluid reaches the condenser and therefore increases efficiency and effectiveness of the system. A preheater may be configured in a chamber upstream of the electrochemical compressor and one or more valves may control the delivery of the superheated fluid to the compressor. A preheater may be configured in an enclosure, having a valve at the inlet and outlet and retain the electrochemically active fluid at a superheated temperature. A preheater may be configured within or attached to a gas diffusion media, flow-filed or current collector and may be in direct communication with the fluid.

Abstract: An electrochemical compression system utilizes an electrolyzer to electrolyze an electrochemically active working fluid, at a first pressure, into decomposition products that are reformed back into said electrochemically active working fluid by a fuel cell, at a higher pressure. Water may be electrolyzed into hydrogen and oxygen and stored in reservoir tanks at an elevated pressure and subsequently provided to a fuel cell for reforming. The hydrogen is provided to the anode side of a polymer electrolyte membrane fuel cell and the oxygen is provided to the cathode side. Water is reformed on the cathode side of the fuel cell at a higher pressure than the inlet to the electrolyzer. This pressure differential enable flow of the electrochemically active working fluid through a conduit from the cathode to the electrolyzer. This flow of fluid may be used in a heat transfer system.

Abstract: An electrochemical compression system utilizes a preheater to heat an electrochemically active working fluid to a superheated temperature delta prior compression. Heating the electrochemically active working fluid to a superheated temperature ensures there will be no condensation before the fluid reaches the condenser and therefore increases efficiency and effectiveness of the system. A preheater may be configured in a chamber upstream of the electrochemical compressor and one or more valves may control the delivery of the superheated fluid to the compressor. A preheater may be configured in an enclosure, having a valve at the inlet and outlet and retain the electrochemically active fluid at a superheated temperature. A preheater may be configured within or attached to a gas diffusion media, flow-filed or current collector and may be in direct communication with the fluid.

Abstract: Refrigeration systems and appliances are provided. A refrigeration system includes a refrigerant, the refrigerant including a working fluid and an electrochemically active fluid. The refrigeration system further includes a condenser, an evaporator, and an electrochemical compressor in fluid communication with the condenser and the evaporator. The refrigeration system can further include various components which advantageously reduce the energy consumption and increase the predicatability and efficiency of the refrigeration system.

Abstract: An electrochemical compression system utilizes an electrolyzer to electrolyze an electrochemically active working fluid, at a first pressure, into decomposition products that are reformed back into said electrochemically active working fluid by a fuel cell, at a higher pressure. Water may be electrolyzed into hydrogen and oxygen and stored in reservoir tanks at an elevated pressure and subsequently provided to a fuel cell for reforming. The hydrogen is provided to the anode side of a polymer electrolyte membrane fuel cell and the oxygen is provided to the cathode side. Water is reformed on the cathode side of the fuel cell at a higher pressure than the inlet to the electrolyzer. This pressure differential enable flow of the electrochemically active working fluid through a conduit from the cathode to the electrolyzer. This flow of fluid may be used in a heat transfer system.