A method for controlling a vapour compression system having an ejector includes, in the case that a pressure difference between a pressure prevailing in the receiver and a pressure of refrigerant leaving the evaporator decreases below a first lower threshold value, the pressure of refrigerant leaving the heat rejecting heat exchanger is kept at a level which is slightly higher than the pressure level providing optimal coefficient of performance.

An ejector refrigeration cycle device includes: a decompressor that decompresses a refrigerant heat-exchanged in a radiator; a first exterior heat exchanger that exchanges heat between the refrigerant decompressed by the decompressor and outside air; an ejector that decompresses the refrigerant flowing out of the radiator in a nozzle portion and draws another refrigerant heat-exchanged in the first exterior heat exchanger; a branch portion in which the refrigerant heat-exchanged in the radiator branches to a side of the decompressor and a side of the nozzle portion; a second exterior heat exchanger that exchanges heat between the refrigerant pressurized in the ejector and the outside air; a bypass portion that causes the refrigerant heat-exchanged in the radiator to flow to the first exterior heat exchanger while bypassing the decompressor and the nozzle portion; and an opening/closing portion that opens or closes the bypass portion.

Embodiments of the present disclosure are directed to a heat exchange device that includes a condenser configured to receive a refrigerant, an evaporator having an evaporation tube bundle, a throttling device configured to receive a first portion of the refrigerant from the condenser and to expand the first portion of the refrigerant before directing the first portion to the evaporator, and an ejector having a high pressure conduit, a low pressure conduit, and an outlet conduit, the ejector is configured to receive the first portion from the throttling device or a second portion of the refrigerant from the condenser via the high pressure conduit, receive a third portion of the refrigerant from the evaporator via the low pressure conduit, mix the first portion or the second portion with the third portion to form a mixed refrigerant, and direct the mixed refrigerant to the evaporator via the outlet conduit.

A refrigerated system includes a heat recovery system defining a heat recovery fluid flow path. The heat recovery system includes an ejector having a primary inlet and a secondary inlet and a first heat exchanger within which heat is transferred between a heat recovery fluid and a secondary fluid. The first heat exchanger is located upstream from the primary inlet of the ejector. A second heat exchanger within which heat is transferred from a heat transfer fluid to the heat recovery fluid is upstream from the secondary inlet of the ejector. At least one recovery heat exchanger is positioned along the heat recovery fluid flow path directly upstream from the first heat exchanger.

An ejector refrigeration circuit comprises a high pressure ejector circuit comprising in the direction of flow of a circulating refrigerant: a heat rejecting heat exchanger/gas cooler having an inlet side and an outlet side; at least two variable ejectors (6, 7) with different capacities connected in parallel, each of the variable ejectors comprising a primary high pressure input port, a secondary low pressure input port and an output port; wherein the primary high pressure input ports of the at least two variable ejectors are fluidly connected to the outlet side of the heat rejecting heat exchanger/gas cooler; a receiver, having an inlet, a liquid outlet, and a gas outlet, wherein the inlet is fluidly connected to the output ports of the at least two variable ejectors; at least one compressor having an inlet side and an outlet side.

The present disclosure relates to a refrigeration cycle apparatus including an ejector capable of significantly increasing the pressure of sucked refrigerant and flowing out the refrigerant having the increased pressure toward a compressor. The ejector 100 includes a drive refrigerant inlet 111 to allow a first refrigerant evaporated in a first evaporator to be introduced, a suction refrigerant inlet 121 to allow a second refrigerant evaporated in a second evaporator to be introduced, a joining portion 131 to join the first refrigerant introduced from the drive refrigerant inlet 111 and the second refrigerant introduced from the suction refrigerant inlet 121, a nozzle neck portion 113 to throttle a flow passage of the first refrigerant introduced from the drive refrigerant inlet 111, and a nozzle diffuser portion 114 including a cylindrical or conical flow passage upstream of the joining portion 131 to allow the first refrigerant that has passed through the nozzle neck portion 113 to pass therethrough, and an inner angle of the nozzle diffuser portion 114 in a plane passing through a center line C is 0 or more and 12 or less.

An apparatus includes an ejector, a first load, a second load, a third load, a first compressor, a second compressor, and an accumulator. The ejector directs a refrigerant to a flash tank that stores the refrigerant. The loads use the refrigerant from the flash tank to cool spaces. The first compressor compresses the refrigerant from the first load. During a defrost cycle, the first compressor directs the refrigerant to the third load to defrost the third load, the accumulator separates the refrigerant that defrosted the third load into a second liquid portion and a second vapor portion, the ejector directs the second liquid portion to the flash tank, and the second compressor compresses the second vapor portion.

A fluid treatment device comprises: a throttling part; a three-way pipe detachably connected to the throttling part; a drainage part detachably connected to the three-way pipe, with one end of the drainage part being provided with an expansion portion, and the throttling part and the drainage part being coaxial; and a separation part, the expansion portion extending into a space enclosed by side walls of the separation part, a fluid flowing in from a first fluid inlet and a fluid flowing in from a second fluid inlet flowing into the separation part through the expansion portion, and the separation part separating the fluids into a gas phase fluid and a liquid phase fluid, wherein the range of an included angle between an axis of the drainage part and an axis of the separation part is 35 degrees to 60 degrees. The fluid treatment device integrates the throttling part, the three-way pipe, the drainage part and the separation part.

An apparatus includes a high side heat exchanger, a flash tank, a first load, a first oil separator, and a first compressor. The high side heat exchanger removes heat from a refrigerant. The flash tank stores the refrigerant. The first load uses the refrigerant to cool a first space proximate the first load. During a first mode of operation, the first oil separator separates an oil from the refrigerant from the first load and directs the refrigerant to an ejector. The ejector directs the refrigerant from the high side heat exchanger and the refrigerant form the first oil separator to the flash tank. The flash tank directs the refrigerant from the first oil separator to the first compressor. The first compressor compresses the refrigerant from the flash tank. During a second mode of operation, the first oil separator directs the oil separated from the refrigerant to the first compressor.

The refrigerant device includes a refrigerant circuit performing a refrigeration cycle in which one of the heat-source-side heat exchanger and the utilization-side heat exchanger serves as a radiator, while the other serves as an evaporator. The refrigerant circuit is filled with a refrigerant including hydrocarbon fluoride having the property of causing disproportional reaction. The refrigerant circuit includes an ejector provided with a depressurization channel, a suction channel and an ejection channel, a gas-liquid separator into which a refrigerant ejected from the ejection channel flows, an expansion mechanism depressurizing a liquid refrigerant flowing from the gas-liquid separator into the evaporator, and a suction pipe guiding a gas refrigerant of the gas-liquid separator into the compressor. As a result, it is possible to reduce the risk of disproportional reaction of the refrigerant.