R-744 SYSTEM WITH HOT GAS DEFROST BY THE TRANSCRITICAL COMPRESSORS

Abstract

A transcritical R-744 refrigeration system with a medium temperature section having a plurality of circuits, at least one evaporator receiving an R-744 refrigerant in a medium-pressure liquid state from a receiver and feeding at least one transcritical compressor to compress the R-744 refrigerant from a low-pressure gaseous state into a high-pressure gaseous state to feed a gas cooler and a throttling device to partially condense the R-744 refrigerant into a medium-pressure gaseous-liquid state, the system comprising a pressure reducing valve connected to a discharge conduit of the at least one transcritical compressor and feeding hot gas to a defrost manifold to defrost one of the plurality of circuits of the medium temperature section, wherein the hot gas being fed to the defrost manifold has a pressure value less than or equal to a maximum operating pressure of the at least one evaporator.

Claims

1. A transcritical R-744 refrigeration system (50) with a medium temperature section (52) having a plurality of circuits, at least one evaporator (11) receiving an R-744 refrigerant in a medium-pressure liquid state from a receiver (8) and feeding at least one transcritical compressor (1) to compress the R-744 refrigerant from a low-pressure gaseous state into a high-pressure gaseous state to feed a gas cooler (5) and a throttling device (7) to partially condense the R-744 refrigerant into a medium-pressure gaseous-liquid state, the system (50) comprising: a pressure reducing valve (41) connected to a discharge conduit (2) of the at least one transcritical compressor (1) and feeding hot gas to a defrost manifold (19) to defrost one of the plurality of circuits of the medium temperature section (52); wherein said hot gas being fed to said defrost manifold (19) has a pressure value less than or equal to a maximum operating pressure of the at least one evaporator (11).

2. The transcritical R-744 refrigeration system (50) of claim 1, further comprising a heat exchanger (43) downstream of said pressure sensing valve (41), said heat exchanger (43) transferring heat from the hot gas fed to the gas cooler (5) to the gas exiting said pressure reducing valve (41).

3. The transcritical R-744 refrigeration system (50) of claim 1, wherein the receiver (8) is a flash tank.

4. The transcritical R-744 refrigeration system (50) of claim 1, wherein the refrigerant exiting the at least one transcritical compressor (1) passes through an oil separator (3) before reaching said pressure reducing valve (41).

5. The transcritical R-744 refrigeration system (50) of claim 1, further comprising an additional defrost manifold (27) in the medium temperature section (52).

6. The transcritical R-744 refrigeration system (50) of claim 1, further comprising a pressure regulating valve (29) to regulate the pressure of the refrigerant before entering the receiver (8).

7. The transcritical R-744 refrigeration system (50) of claim 1, further comprising a plurality of check valves (36, 39) to prevent any hot gas from entering a liquid line.

8. The transcritical R-744 refrigeration system (50) of claim 1, further comprising a safety valve (46) connected to said defrost manifold (19).

9. The transcritical R-744 refrigeration system (50) of claim 1, further comprising a low temperature section (54) comprising an evaporator (12) receiving an R-744 refrigerant from the receiver (8) and feeding at least one subcritical compressor (20), wherein said hot gas is further fed to a defrost manifold (18) in said low temperature section (54) to defrost one of a plurality of circuits of said low temperature section (54).

10. The transcritical R-744 refrigeration system (50) of claim 8, further comprising an additional defrost manifold (26) in the low temperature section (54).

11. A method of defrosting one of a plurality of circuits of a transcritical R-744 refrigeration system (50) with a medium temperature section (52) having a plurality of circuits, at least one evaporator (11) receiving an R-744 refrigerant in a medium-pressure liquid state from a receiver (8) and feeding at least one transcritical compressor (1) to compress the R-744 refrigerant from a low-pressure gaseous state into a high-pressure gaseous state to feed a gas cooler (5) and a throttling device (7) to partially condense the R-744 refrigerant into a medium-pressure gaseous-liquid state, the method comprising the steps of: activating a pressure reducing valve connected to a discharge conduit (2) of the at least one transcritical compressor (1); and feeding hot gas from the at least one transcritical compressor (1) to a defrost manifold (19) in the medium temperature section (52) to defrost one of the plurality of circuits of the medium temperature section (52); wherein said hot gas being fed to said defrost manifold (19) has a pressure value less than or equal to a maximum operating pressure of the at least one evaporator (11).

12. A method of defrosting one of a plurality of circuits of a transcritical R-744 refrigeration system (50) with a medium temperature section (52) and a low temperature section (54) each having a plurality of circuits, a plurality of evaporators (11, 12) receiving an R-744 refrigerant in a medium-pressure liquid state from a receiver (8) and feeding at least one transcritical compressor (1) and at least one subcritical compressor (20) to compress the R-744 refrigerant from a low-pressure gaseous state into a high-pressure gaseous state to feed a gas cooler (5) and a throttling device (7) to partially condense the R-744 refrigerant into a medium-pressure gaseous-liquid state, the method comprising the steps of: activating a pressure reducing valve connected to a discharge conduit (2) of the at least one transcritical compressor (1); and feeding hot gas from the at least one transcritical compressor (1) to at least one defrost manifold (18, 19) in at least one of the medium temperature section (52) and the low temperature section (54) to defrost one of the plurality of circuits; wherein said hot gas being fed to said at least one defrost manifold (18, 19) has a pressure value less than or equal to a maximum operating pressure of the plurality of evaporators (11, 12).

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0020] FIG. 1 is a schematic view of a transcritical R-744 refrigeration system having hot gas defrost provided by the transcritical R-744 compressors, in accordance with an illustrative embodiment of the present invention.

DETAILED DESCRIPTION OF THE ILLUSTRATIVE EMBODIMENTS

[0021] Referring to FIG. 1, there is shown a transcritical R-744 refrigeration system, generally referred to using the reference numeral 50, that uses the system's transcritical compressors to perform hot gas defrost, in accordance with an embodiment of the present invention. In an embodiment, system 50 comprises both a medium temperature section 52 and a low temperature section 54. In an alternate embodiment, system 50 comprises only a medium temperature section 52, thus negating then need for a low temperature section 54.

[0022] The refrigeration cycle begins at transcritical compressors 1, where refrigerant R-744 vapors are compressed by transcritical compressors 1 and then fed through conduit 2, oil separator 3, conduit 44, optional heat exchanger 43 (useful in applications such as large factories with low temperatures and large coils) and conduit 4 to gas cooler 5 where their temperature is reduced due to heat transfer with the ambient air. Then, the R-744 vapors, whose temperature has been reduced while pressure remains high, are fed through conduit 6 to throttling device 7, where both their pressure and temperature are reduced, thus provoking partial liquification. After the throttling device 7, the mixture of vapors and liquid are fed to the receiver 8 where separation of the vapors from the liquid occurs. The vapors from receiver 8 are fed through pressure regulating valve 34 to the suction of the transcritical compressors 1. In alternate embodiments, receiver 8 is a flash tank and pressure regulating valve 34 is a flash gas bypass valve. The resulting liquid from receiver 8 is fed to the medium temperature section 52 of the system 50 through conduit 9, expansion valves 32 and evaporators 11. As a person of ordinary skill in the art would understand, as the liquid refrigerant passes through evaporators 11, it absorbs heat from the ambient air and changes states back to vapor, thus cooling the ambient air. Then, the R-744 vapors returns to transcritical compressors 1 to restart the refrigeration cycle.

[0023] In the embodiment where system 50 comprises a low temperature section 54, the resulting liquid from receiver 8 is also fed through conduit 10, expansion valves 33 and evaporators 12. After the evaporation process at evaporators 12 which provides refrigeration to the ambient air, low-pressure R-744 vapors are fed through suction manifold 15 and compressor suction conduit 16 to the suction port of low temperature or subcritical compressors 20. The R-744 vapors compressed by subcritical compressors 20 are fed through conduit 17 directly to the suction manifold 13 and through compressor suction conduits 14 to join the R-744 vapors from the medium temperature section 52 as they enter transcritical compressors 1 to restart the refrigeration cycle.

[0024] Still referring to FIG. 1, when defrosting is required for a given circuit in the system 50 in either the medium temperature section 52 or the low temperature section 54 (in the embodiment that comprises a low temperature section), an electronically operated pressure reducing valve 41 is activated. High temperature and high-pressure vapors are fed from transcritical compressors 1 through conduit 40 and pressure reducing valve 41, where their pressure is reduced to a level that is compatible with the certified maximum operating pressure of evaporators 11, 12 and that corresponds to a R-744 vapor condensing temperature that is higher than the freezing point of water.

[0025] As the vapors exit pressure reducing valve 41, their temperature is reduced due to throttling, which can influence the effectiveness of the defrosting process. Thus, in an alternate embodiment, to recuperate a considerable portion of this temperature loss, the vapors from pressure reducing valve 41 are fed through conduit 42 to heat exchanger 43 where the vapors are reheated by heat transfer with the rest of the hot high-pressure vapors.

[0026] Still referring to FIG. 1, the R-744 vapors from pressure reducing valve 41 (or from heat exchanger 43 in the above-mentioned alternate embodiment) are fed through conduit 45, defrost manifold 18 or 19 and valve 31 to the suction line of the circuit requiring defrosting. At this point, the electronic expansion valves 32 or 33 and the suction stop valve 35 are closed. The R-744 vapors are then fed through evaporator 11 or 12, check valve 36, conduits 37, 38, defrost manifold 26 or 27 and conduit 28 to pressure regulating valve 29, and then through conduit 30 to the receiver (flash tank) 8. Check valve 39 is used to prevent the hot gas from entering the liquid line, which is necessary due to the low pressure of the R-744 refrigerant. Valve 29 maintains the pressure in conduit 28 to be higher than the pressure in receiver (flash tank) 8 to ensure the return of the condensate from the circuit having been defrosted to the receiver 8. Valve 46 serves as a safety valve in case of a rapid surge of the defrost pressure.

[0027] Advantageously, transcritical R-744 refrigeration system 50 provides more efficient defrosting than previous R-744 refrigeration systems and is less costly as it requires less valves and no oil separator for the low temperature section 54. Further, system 50 is less complicated than previous R-744 refrigeration systems and can defrost larger circuits, thus requiring less circuits overall. Further, in an alternative embodiment, as defrosting is provided by transcritical compressors 1, system 50 only comprises a medium temperature section 52, negating the use for low temperature section 54. Further, in the embodiment where the system 50 comprises only a medium temperature section 52, the system 50 requires less components as there is no need for a low temperature section 54.

[0028] The scope of the claims should not be limited by the preferred embodiments set forth in the examples, but should be given the broadest interpretation consistent with the description as a whole.