The present invention regards a thermally driven, environmental control unit including, in a closed fluid-flow, non-pressurized circuit, a mixing heat exchanger, a heat recovery unit, a fractionator/evaporator, and one or more condensers. The system is designed to include at least one solute and a solvent, selected so that the mixture of each solute and the solvent produce an enthalpy change of between about 5 to 30 kJ/mol for cooling and 10 to 200 kJ/mol for heating. A plurality of pumps is integrated into the system to move the solute and the solvent, and a mixture thereof, among the various components of the present invention. The unit further includes a liquid loop coupled with the mixing heat exchanger and an air handler to provide warm or cool supply air. The present invention further regards a process for cooling or heating air using enthalpy change of solution associated with the dissolution of a solute in a solvent, at relatively constant atmospheric pressure, and separation of the solute from the solvent for re-use in the process.

The present disclosure relates to an absorption cooling machine including an absorber, a first regenerator, a second regenerator, a condenser, an expansion device, and an evaporator, and relates to a cooling machine that prevents the refrigerant from flowing backward to the first regenerator under a low pressure condition by installing a gas-liquid separator that separates the refrigerant discharged from the first and second regenerators and flows into the condenser into a gas state and a liquid state, in order to heat the absorption solution supplied from the absorber to separate into a refrigerant and an absorbent, and to smoothly discharge the refrigerant from the first regenerator and the second regenerator for discharging the separated refrigerant to the condenser.

The present disclosure relates to an absorption cooling machine including an absorber, a first regenerator, a second regenerator, a condenser, an expansion device, and an evaporator, and relates to a cooling machine that prevents the refrigerant from flowing backward to the first regenerator under a low pressure condition by installing a gas-liquid separator that separates the refrigerant discharged from the first and second regenerators and flows into the condenser into a gas state and a liquid state, in order to heat the absorption solution supplied from the absorber to separate into a refrigerant and an absorbent, and to smoothly discharge the refrigerant from the first regenerator and the second regenerator for discharging the separated refrigerant to the condenser.

A heat exchanging device includes a regenerator that heats an absorbent by external energy and generates a vapor refrigerant by evaporating a refrigerant from the absorbent, a condenser that generates a liquid refrigerant by cooling and liquefying the vapor refrigerant, an evaporator that generates a vapor refrigerant by vaporizing the vapor refrigerant, an absorber that absorbs the liquid refrigerant into the absorbent, and first and second cover members arranged opposite to each other. The evaporator absorbs heat from a space on a second cover member side in a space between the first and second cover members through the second cover member. The absorber dissipates the heat from a space on a first cover member side in the space between the first and second cover members through the first cover member, and circulates the refrigerant and the absorbent.

A heat exchanging device includes a regenerator that heats an absorbent by external energy and generates a vapor refrigerant by evaporating a refrigerant from the absorbent, a condenser that generates a liquid refrigerant by cooling and liquefying the vapor refrigerant, an evaporator that generates a vapor refrigerant by vaporizing the vapor refrigerant, an absorber that absorbs the liquid refrigerant into the absorbent, and first and second cover members arranged opposite to each other. The evaporator absorbs heat from a space on a second cover member side in a space between the first and second cover members through the second cover member. The absorber dissipates the heat from a space on a first cover member side in the space between the first and second cover members through the first cover member, and circulates the refrigerant and the absorbent.

The invention relates to a process for dehumidifying a moist gas mixture. The invention further relates to an apparatus for dehumidifying a moist gas mixture and to the use of said apparatus in the process according to the invention.

The invention relates to a process for dehumidifying a moist gas mixture. The invention further relates to an apparatus for dehumidifying a moist gas mixture and to the use of said apparatus in the process according to the invention.

The present invention regards a thermally driven, environmental control unit including, in a closed fluid-flow, non-pressurized circuit, a mixing heat exchanger, a heat recovery unit, a fractionator/evaporator, and one or more condensers. The system is designed to include at least one solute and a solvent, selected so that the mixture of each solute and the solvent produce an enthalpy change of between about 5 to 30 kJ/mol for cooling and 10 to 200 kJ/mol for heating. A plurality of pumps are integrated into the system to move the solute and the solvent, and a mixture thereof, among the various components of the present invention. The unit further includes a liquid loop coupled with the mixing heat exchanger and an air handler to provide warm or cool supply air. The present invention further regards a process for cooling or heating air using enthalpy change of solution associated with the dissolution of a solute in a solvent, at relatively constant atmospheric pressure, and separation of the solute from the solvent for re-use in the process.

The present invention regards a thermally driven, environmental control unit including, in a closed fluid-flow, non-pressurized circuit, a mixing heat exchanger, a heat recovery unit, a fractionator/evaporator, and one or more condensers. The system is designed to include at least one solute and a solvent, selected so that the mixture of each solute and the solvent produce an enthalpy change of between about 5 to 30 kJ/mol for cooling and 10 to 200 kJ/mol for heating. A plurality of pumps are integrated into the system to move the solute and the solvent, and a mixture thereof, among the various components of the present invention. The unit further includes a liquid loop coupled with the mixing heat exchanger and an air handler to provide warm or cool supply air. The present invention further regards a process for cooling or heating air using enthalpy change of solution associated with the dissolution of a solute in a solvent, at relatively constant atmospheric pressure, and separation of the solute from the solvent for re-use in the process.

A liquid desiccant system including a high desorber, a low desorber, and an absorber that are in fluid communication with a working solution, where the high desorber provides rejected water vapor from the working fluid for condensation in a condenser of the low desorber that provides heat for rejection of additional water from the working solution in the low desorber effectively multiplying the heat provided for desorption. The low desorber provided the concentrated working solution to the absorber where water from ambient air is condensed into the concentrated working solution to provide a dilute working solution within a working solution conduit of the absorber that is thermally coupled to an internal cooler of the absorber. In some embodiments, the working solution can be an aqueous solution of at least one ionic liquid.