A plate apparatus suitable for heat and/or material exchange has plates (P.sub.0, P.sub.1, P.sub.2, P.sub.3) contacting each other flush along a peripheral seal (1) while forming respective intermediate spaces (Z.sub.0, Z.sub.1, Z.sub.2, Z.sub.3) and having upper (2, 3) and lower (4, 5) through-flow openings for fluids. A group of these upper and lower through-flow openings (2, 5) is allocated to at least two fluids and is connected by correspondingly placed seals to every second plate intermediate space (Z.sub.1, Z.sub.3) carrying a flow from top to bottom. In flush upper through-flow openings (2) of plates (P.sub.0, P.sub.1, P.sub.2, P.sub.3) a distribution lance (6) runs across these openings and has outlet openings (6a) for at least one of the fluids. It is essential that the outlet openings (6a) are directed into those plate intermediate spaces (Z.sub.0, Z.sub.2) arranged between the second plate intermediate spaces (Z.sub.1, Z.sub.3) for the fluids to be mixed.

The method combines different electrolyte solutions having the same solvent. The solution is successively compressed and vaporized at different temperatures and the vapor is successively absorbed by the second solution that exhibits higher negative deviation, at higher temperature. The absorption heat of each absorber is recovered by the next evaporator. The more evaporator-absorber pairs that are used the higher the temperature lift or the created pressure ratio. Finally the vapor returns to the first solution at high temperature. Electrolyte is dissolved and rejected from each solution to achieve total heat recovering and the very high efficiency of the cycle. Gas absorption is suggested instead of solvent vapor.

The present invention relates to a triple-effect absorption chilling apparatus adopting a structure of an anti-parallel cycle in which an absorber and a first regenerator are connected in series, a second regenerator and a third regenerator are connected in parallel with the first regenerator, and the solution through the second regenerator and the third regenerator is returned to the absorber. Therefore, according to the present invention, it is possible to improve efficiency by acquiring a higher coefficient of performance than conventional absorption refrigerators, and to reduce energy consumption.

An intermittent operation based continuous absorption system (IOBCAS) which supports cooling effect during the daytime without the use of a solution pump is provided. The IOBCAS may utilize an isochoric process for pressurization of the system and the system may include a plurality of generator-absorber units that intermittently operate in succession to provide a continuous refrigeration cooling effect during the daytime. The system of the present disclosure enables the plurality of generator-absorber units to switch between a generation, absorption, and heat recovery mode of operation to provide cooling effect during the daytime which a higher coefficient of performance compared with conventional intermittent system.

In one embodiment, the present invention relates to the use of ionic liquids and gas refrigerants in a refrigerant composition in a temperature adjustment system, such as a refrigeration system.

The invention relates to an apparatus (1) comprising a generator (5), an evaporator (6), an absorber (8) and a condenser (9) circulating a refrigerant (R), an inert (I) and an absorbent (A) in a diffusion-absorption cycle. The generator (5) and the evaporator (6) are arranged in an electric cabinet (2) to receive a heat load from primary electric components (3) and secondary electric components (4). The absorber (8) and the condenser (9) are arranged outside of the electric cabinet (2) and at a higher level than the evaporator (6) to receive fluid from the generator (5) and the evaporator (6) and for dissipating heat from the received fluid to the surrounding environment. The inert (I) and refrigerant (R) are selected such that the inert (I) is heavier than the refrigerant (R) in order to obtain fluid circulation where the inert (I) exiting the absorber (8) flows downwards to the evaporator (6) and the inert (I) exiting the evaporator (6) flows upwards to the absorber (8).

Disclosed is a refrigeration system, which may include a generator, a condenser, an evaporator, and an absorber connected in sequence, the condenser being disposed above the evaporator, and the absorber being disposed below the evaporator; the evaporator includes an outer pipe, a hydrogen inlet pipe, and a liquid ammonia pipe; one end of the outer pipe is sealed and the other end thereof is connected to the absorber; the diameter of the end of the outer pipe connected to the absorber is gradually reduced facing a direction of the absorber; the hydrogen inlet pipe is hidden inside the outer pipe; an air outlet end of the hydrogen inlet pipe is disposed at the sealed end of the outer pipe.

A method for real-time detecting and dealing with ammonia leakage of a mini diffusion-absorption ammonia refrigerating apparatus used for refrigerators, wine cabinets or freezers comprising a main container body; the rear portion of the main container body is provided with a mini diffusion-absorption ammonia refrigerating apparatus; at least one high-sensitivity ammonia sensor is disposed in the refrigerating apparatus; the ammonia sensor is connected to a control panel; after detecting the concentration of ammonia gas, collecting and processing the data, many means can be initiated to prevent ammonia gas from being leaked, achieving a precise judgement and an effective treatment.

A system may include a beverage compartment with a beverage positioned therein, a wetted material disposed about the beverage, at least one sorption cartridge, and a vacuum pump. The sorption cartridge may be in communication with the beverage compartment, and the vacuum pump may be in communication with the sorption cartridge to create a vacuum in the sorption cartridge and the beverage compartment, causing water to evaporate from the wetted material and be captured by the sorption cartridge, thereby lowering the temperature of the wetted material and in turn cooling the beverage. In some instances, the sorption cartridge may be detached from the vacuum pump and the beverage compartment to discharge the captured water therein by way of solar energy. In other instances, the sorption cartridge may be in communication with a heater assembly to blow heated air through the sorption cartridge to discharge the captured water therein.

A system includes an electrochemical regenerator configured to receive a first solution having a first salt concentration and output a second solution having a second salt concentration lower than the first salt concentration and a third solution having a third salt concentration higher than the first salt concentration. The first and second solutions are sent to first and second reservoirs respectively absorb and emit heat in response to a phase change of one of the solutions. The absorption or emission of heat can be used in a heat pump system.