There is disclosed a heat-transferring device comprising a buffer tank (1), a reactor vessel (2) in thermal contact with the buffer tank, wherein an active substance is held inside the reactor vessel, a burner (A), a reactor heating loop adapted to transfer heat from the burner to the active substance in the reactor vessel, a reactor cooling loop adapted to transfer heat from the active substance in the reactor vessel to the buffer tank, a volatile liquid reservoir (14) in fluid contact with the reactor vessel, an evaporator (15) in fluid contact with the volatile liquid reservoir, a volatile liquid in the volatile liquid reservoir, with the ability to be absorbed by the active substance at a first temperature and desorbed by the active substance at a higher temperature, an exhaust gas pipe (10,11,12) from the burner to the volatile liquid reservoir to heat it.

An absorption heating and cooling system having an absorber, which allows the gaseous refrigerant to be absorbed by the absorbent, condensed by its heat, and thus the liquefaction of the gaseous refrigerant while the heating operation takes place, and an evaporator that allows the liquid refrigerant to evaporate by heating and thus cooling process to be carried out, wherein a separation unit using a method of separation by solidification employed which works through the icing/crystallization/freezing methods and which enables the separation the refrigerant-absorbent mixture.

A space vehicle is described. The space vehicle comprises one or more heat-producing components, and a closed loop cooling system configured to remove heat generated by the one or more heat-producing components. The closed loop cooling system comprises a coolant passageway defining a closed loop, a coolant located within the coolant passageway, the coolant comprising a static pressure of 100 pounds per square inch or lower and the coolant being in a single liquid phase through the coolant passageway, and one or more pumps configured to move the coolant through the coolant passageway. The closed loop cooling system further comprises a first heat exchange component disposed along the coolant passageway, the first heat exchange component configured to transfer heat from the heat-producing components to the coolant, and a second heat exchange component disposed along the coolant passageway, the second heat exchange component configured to remove heat from the coolant.

A molecular sieve chamber comprises a plurality of containers generally parallel to another and arranged in a matrix having adjacent rows that may be offset from one another. The plurality of containers may be spaced from one another forming a plurality of tortuous air passages from a first side of the molecular sieve chamber to a second side of the molecular sieve chamber opposite the first side. Each of the plurality of containers may include a venting passage having a plurality of apertures, and at least one molecular sieve positioned between the venting passage and a solid sidewall. A fan may be configured to blow air between the plurality of containers in a direction generally perpendicular to a longitudinal axis of the plurality of containers. The venting passages of each of the plurality of containers may be fluidly coupled to one another.

A molecular sieve chamber comprises a plurality of containers generally parallel to another and arranged in a matrix having adjacent rows that may be offset from one another. The plurality of containers may be spaced from one another forming a plurality of tortuous air passages from a first side of the molecular sieve chamber to a second side of the molecular sieve chamber opposite the first side. Each of the plurality of containers may include a venting passage having a plurality of apertures, and at least one molecular sieve positioned between the venting passage and a solid sidewall. A fan may be configured to blow air between the plurality of containers in a direction generally perpendicular to a longitudinal axis of the plurality of containers. The venting passages of each of the plurality of containers may be fluidly coupled to one another.

The present invention relates to an absorption chiller which comprises an evaporator, an absorber, a regenerator and a condenser and has an absorbing solution and a refrigerant circulating. A heat transfer pipe, which is provided on one or more of the evaporator, absorber, regenerator and condenser, is comprised, and a ductile stainless steel pipe, which has 1% or less of delta ferrite matrix structure on the basis of the grain size area, is applied to the heat-transfer pipe. Therefore, copper-level flexibility can be obtained in comparison with an existing stainless steel pipe.

The present invention relates to an absorption chiller which comprises an evaporator, an absorber, a regenerator and a condenser and has an absorbing solution and a refrigerant circulating. A heat transfer pipe, which is provided on one or more of the evaporator, absorber, regenerator and condenser, is comprised, and a ductile stainless steel pipe, which has 1% or less of delta ferrite matrix structure on the basis of the grain size area, is applied to the heat-transfer pipe. Therefore, copper-level flexibility can be obtained in comparison with an existing stainless steel pipe.

The invention relates to a heat exchanger having at least one sorption duct in which is arranged a sorption medium and through which a fluid can be made to flow, characterized in that the heat exchanger also contains at least one catalyst with which a fuel can be converted exothermically such that at least some of the resulting heat can be conveyed to the sorption medium. The invention also relates to a method for heating and/or conditioning a gas stream, having at least the following steps: supplying a gas stream, containing multiple different components, into a sorption duct in which is arranged a sorption medium, such that at least one component is bound in the sorption medium, and supplying and exothermically converting at least one fuel under the action of a catalyst, such that at least one component of the gas stream is expelled from the sorption medium.

The invention relates to a heat exchanger having at least one sorption duct in which is arranged a sorption medium and through which a fluid can be made to flow, characterized in that the heat exchanger also contains at least one catalyst with which a fuel can be converted exothermically such that at least some of the resulting heat can be conveyed to the sorption medium. The invention also relates to a method for heating and/or conditioning a gas stream, having at least the following steps: supplying a gas stream, containing multiple different components, into a sorption duct in which is arranged a sorption medium, such that at least one component is bound in the sorption medium, and supplying and exothermically converting at least one fuel under the action of a catalyst, such that at least one component of the gas stream is expelled from the sorption medium.

The present invention pertains to systems, methods, and compositions for liquid phase change, including for active cloud point, e.g., critical solution temperature, adjustment and heating or cooling, e.g., refrigeration, cycles. In some embodiments heat is absorbed, released or both due to phase changes in a liquid system. Advantageously, the phase changes may be controlled by controlling the ingredients or amounts of certain components of the liquid system. Advantages may include lower capital expenditures, lower operating expenses, or both for a diverse and wide range of heating and cooling applications. Such applications include, for example, cooling of data centers, cooled transportation of goods, refrigeration, heat pumps, extractions, ocean thermal energy conversion, and de-icing of roads to name just a few.