Vapor compression system and method for controlling conditions in ambient surroundings
A vapor compression system including an evaporator, a compressor, and a condenser interconnected in a closed-loop system and a method of operating such a system. The method includes the conversion of expanded liquid heat transfer fluid from a liquid form to a high quality liquid vapor mixture before delivery to the evaporator. In one embodiment, the heat transfer surface of the evaporator coil is smaller than that required to obtain an equivalent evaporator capacity when the expanded liquid heat transfer fluid is not converted from a liquid form to a high quality liquid vapor mixture
1. A method of operating a vapor compression system, comprising:
compressing a heat transfer fluid in a compressor;
condensing the heat transfer fluid in a condenser;
expanding the heat transfer fluid in an expansion device to form an expanded heat transfer fluid;
supplying the expanded heat transfer fluid to an evaporator feed line;
converting a portion of a liquid form of the expanded heat transfer fluid to a high quality liquid vapor mixture;
supplying the high quality liquid vapor mixture to an evaporator coil having a heat transfer surface,
converting a portion of a liquid form of the high quality liquid vapor mixture to a vapor form within the evaporator coil; and
returning the heat transfer fluid to the compressor by a suction line,
wherein, at a fixed cooling load, the heat transfer surface of the evaporator coil is smaller than that required to obtain an equivalent evaporator capacity when the portion of the liquid form of the expanded heat transfer fluid is not converted from the liquid form to the high quality liquid vapor mixture.
2. The method of claim 1 , wherein at least one of the compressor, the expansion device, a diameter of the evaporator feed line, and a length of the evaporator feed line is configured to convert the portion of the liquid form of the expanded liquid heat transfer fluid to the high quality liquid vapor mixture.
3. The method of claim 1 , wherein a length of the evaporator coil is shorter than that required to obtain an equivalent evaporator capacity when the portion of the liquid heat transfer fluid is not converted from the liquid form to the high quality liquid vapor mixture.
4. The method of claim 1 , wherein the heat transfer fluid received by the evaporator coil is a saturated vapor.
5. The method of claim 1 , wherein the heat transfer fluid is received by the evaporator coil in a turbulent state.
6. The method of claim 1 , wherein the expansion device forms part of a multifunctional valve.
7. The method of claim 1 , wherein the expansion device forms part of a recovery valve.
8. The method of claim 1 , wherein a temperature sensor is mounted to the suction line and is operatively connected to the expansion device.
9. The method of claim 8 , wherein the heat transfer fluid undergoes expansion at the expansion device at a rate determined by a temperature of the suction line at the temperature sensor.
10. The method of claim 1 , wherein the heat transfer fluid expanded within the expansion device is not passed through a distributor before delivery to the evaporator coil.
11. A method of operating a vapor compression system, comprising:
compressing a heat transfer fluid in a compressor;
condensing the heat transfer fluid in a condenser;
expanding the heat transfer fluid in an expansion device to form an expanded heat transfer fluid and supplying the expanded heat transfer fluid to an evaporator feed line;
converting a portion of a liquid form of the expanded heat transfer fluid to a high quality liquid vapor mixture;
supplying the high quality liquid vapor mixture to an evaporator coil,
converting a portion of a liquid form of the high quality liquid vapor mixture to a vapor form within the evaporator coil; and
returning the heat transfer fluid to the compressor by a suction line,
wherein, at a fixed cooling load, the conversion of the portion of the liquid heat transfer fluid from a liquid form to a high quality liquid vapor mixture allows for at least an equivalent evaporator capacity to be achieved using a decreased heat transfer fluid load when compared to a heat transfer fluid load required when the portion of the liquid form of the expanded heat transfer fluid is not converted from the liquid form to the high quality liquid vapor mixture.
12. The method of claim 11 , wherein at least one of the compressor, the expansion device, a diameter of the evaporator feed line, and a length of the evaporator feed line is configured to convert the portion of the liquid form of the expanded liquid heat transfer fluid to the high quality liquid vapor mixture.
13. The method of claim 11 , wherein the heat transfer fluid received by the evaporator coil is a saturated vapor.
14. The method of claim 11 , wherein the heat transfer fluid is received by the evaporator coil in a turbulent state.
15. The method of claim 11 , wherein the expansion device forms part of a multifunctional valve.
16. The method of claim 11 , wherein the expansion device forms part of a recovery valve.
17. The method of claim 11 , wherein a temperature sensor is mounted to the suction line and is operatively connected to the expansion device.
18. The method of claim 17 , wherein the heat transfer fluid undergoes expansion at the expansion device at a rate determined by a temperature of the suction line at the temperature sensor.
19. The method of claim 11 , wherein the heat transfer fluid expanded within the expansion device is not passed through a distributor before delivery to the evaporator coil.
20. The method of claim 11 , wherein at least a portion of the vapor compression fluid entering the compressor is in a liquid state.
21. A method of operating a vapor compression system, comprising:
compressing a heat transfer fluid in a compressor;
condensing the heat transfer fluid in a condenser;
expanding the heat transfer fluid in an expansion device to form an expanded heat transfer fluid and supplying the expanded heat transfer fluid to an evaporator feed line;
converting a portion of a liquid form of the expanded liquid heat transfer fluid to a high quality liquid vapor mixture;
supplying the high quality liquid vapor mixture to an evaporator coil,
converting a portion of a liquid form of the high quality liquid vapor mixture to a vapor form within the evaporator coil; and
returning the heat transfer fluid to the compressor by a suction line,
wherein, operating at a fixed cooling load, the conversion of the portion of the liquid heat transfer fluid from a liquid form to a high quality liquid vapor mixture allows for at least an equivalent evaporator capacity to that achieved when the portion of the liquid form of the expanded heat transfer fluid is not converted from the liquid form to the high quality liquid vapor mixture and wherein a distributor is present between the evaporator feed line and the evaporator coil.
22. The method of claim 21 , wherein at least one of the compressor, the expansion device, a diameter of the evaporator feed line, and a length of the evaporator feed line is configured to convert the portion of the liquid form of the expanded liquid heat transfer fluid to the high quality liquid vapor mixture.
23. The method of claim 21 , wherein the heat transfer fluid received by the evaporator coil is a saturated vapor.
24. The method of claim 21 , wherein the heat transfer fluid is received by the evaporator coil in a turbulent state.
25. The method of claim 21 , wherein the expansion device forms part of a multifunctional valve.
26. The method of claim 21 , wherein the expansion device forms part of a recovery valve.
27. The method of claim 21 , wherein a temperature sensor is mounted to the suction line and is operatively connected to the expansion device.
28. The method of claim 27 , wherein the heat transfer fluid undergoes expansion at the expansion device at a rate determined by a temperature of the suction line at the temperature sensor.