Air cooled chiller with heat recovery
View Patent ↗Air cooled chillers have auxiliary heat recovery systems that include a heat recovery heat exchanger for transferring heat from a compressed refrigerant to a process fluid. According to certain embodiments, the air cooled chillers also includes a compressor, a condenser, an expansion device, and a controller to govern operations of the expansion device, a fan in the condenser, and other components of the chiller system. The controller may receive signals from temperature and pressure sensors located throughout the chiller system in order to determine a heat recovery load of the heat recovery heat exchanger. The controller may govern operations of the condenser fan and the expansion device according to a low heat recovery mode, an intermediate heat recovery mode, or a full heat recovery mode. In full heat recovery mode, the controller operates the expansion device based on subcooling detected in the heat recovery heat exchanger.
1. A refrigeration system comprising:
an evaporator configured to cool a cooling fluid via heat exchange with a refrigerant;
a compressor configured to receive the refrigerant from the evaporator and compress the refrigerant;
a heat recovery heat exchanger configured to receive the compressed refrigerant and transfer heat from the compressed refrigerant to a process fluid;
a condenser configured to receive and to condense the compressed refrigerant from the heat recovery heat exchanger;
an expansion valve configured to expand the condensed refrigerant; and
a controller configured to:
compare a temperature of the process fluid exiting the heat recovery heat exchanger to a setpoint temperature, wherein the controller is configured to determine a heat recovery demand when a difference between the temperature and the setpoint temperature exceeds a threshold;
operate the refrigeration system in a heat recovery mode of a plurality of heat recovery modes in response to determining the heat recovery demand, wherein the controller is configured to determine the heat recovery mode based on a heat recovery load, wherein the heat recovery load is determined by comparing a determined amount of heat transferred from the refrigerant to the process fluid through the heat recovery heat exchanger with an amount of heat available from the refrigerant flowing through the refrigeration system; and
increase a flow of the process fluid through the heat recovery heat exchanger, decrease a fan speed of the condenser, and control the expansion valve in response to determining an increase in the heat recovery load.
2. The refrigeration system of claim 1 , wherein the controller is configured to determine the heat recovery load by calculating the amount of heat transferred from the refrigerant to the process fluid as a percentage of a value for an amount of heat transferred from the cooling fluid to the refrigerant in the evaporator added to an amount of power input to the compressor.
3. The refrigeration system of claim 2 , comprising a temperature sensor configured to measure the temperature of the process fluid exiting the heat recovery heat exchanger.
4. The refrigeration system of claim 2 , wherein the controller is configured to operate in a low heat recovery mode of the plurality of heat recovery modes by controlling the fan speed at a speed appropriate for normal chiller operation, controlling the expansion valve to maintain a level of subcooling of the refrigerant exiting the condenser, and maintaining a bypass valve to control flow of the process fluid through the heat recovery heat exchanger.
5. The refrigeration system of claim 2 , wherein the controller is configured to operate in an intermediate heat recovery mode of the plurality of heat recovery modes by controlling the fan speed based on a lower of a speed calculated based on normal chiller operation and a speed calculated based on a temperature at a process fluid exit of the heat recovery heat exchanger, controlling the expansion valve based on a larger of a value calculated based on refrigerant leaving the condenser and refrigerant leaving the heat recovery heat exchanger, and controlling a bypass valve to initially open to allow full flow of the process fluid through the heat recovery heat exchanger.
6. The refrigeration system of claim 2 , wherein the controller is configured to operate in a full heat recovery mode of the plurality of heat recovery modes by controlling the fan speed at a speed calculated based on a temperature at a process fluid exit of the heat recovery heat exchanger, controlling the expansion valve to maintain a level of subcooling of the refrigerant exiting the heat recovery heat exchanger, and controlling a bypass valve to initially open to allow full flow of the process fluid through the heat recovery heat exchanger.
7. The refrigeration system of claim 2 , wherein the controller is configured to operate in a low heat recovery mode of the plurality of heat recovery modes when the calculated amount of heat transferred from the refrigerant to the process fluid as a percentage of a value for an amount of heat transferred from the cooling fluid to the refrigerant in the evaporator added to an amount of power input to the compressor is approximately between 0 and 50 percent.
8. The refrigeration system of claim 2 , wherein the controller is configured to operate in an intermediate heat recovery mode of the plurality of heat recovery modes when the calculated amount of heat transferred from the refrigerant to the process fluid as a percentage of a value for an amount of heat transferred from the cooling fluid to the refrigerant in the evaporator added to an amount of power input to the compressor is approximately between 50 and 80 percent.
9. The refrigeration system of claim 2 , wherein the controller is configured to operate in a full heat recovery mode of the plurality of heat recovery modes when the calculated amount of heat transferred from the refrigerant to the process fluid as a percentage of a value for an amount of heat transferred from the cooling fluid to the refrigerant in the evaporator added to an amount of power input to the compressor is approximately between 80 and 100 percent.
10. A refrigeration system, comprising:
a compressor configured to compress a refrigerant;
a heat recovery heat exchanger configured to receive the compressed refrigerant and transfer heat from the compressed refrigerant to a process fluid;
a condenser configured to receive and to condense the compressed refrigerant;
an expansion valve configured to expand the condensed refrigerant;
an economizer configured to receive the expanded refrigerant and to at least partially vaporize the refrigerant;
an evaporator configured to receive refrigerant from the economizer and to vaporize the refrigerant;
a temperature sensor configured to sense a temperature of the process fluid exiting the heat recovery heat exchanger; and
a controller coupled to the temperature sensor and configured to:
compare the sensed temperature of the process fluid exiting the heat recovery heat exchanger to a setpoint temperature and, in response to a difference between the sensed temperature and the setpoint temperature exceeding a threshold, determine a heat recovery demand;
operate in a heat recovery mode of a plurality of heat recovery modes in response to determining the heat recovery demand, wherein the controller is configured to determine the heat recovery mode based at least in part on a heat recovery load, wherein the heat recovery load is determined by comparing a determined amount of heat transferred from the refrigerant to the process fluid through the heat recovery heat exchanger with an amount of heat transferred from a cooling fluid to the refrigerant in the evaporator; and
increase a flow of the process fluid through the heat recovery heat exchanger, decrease a fan speed of the condenser, and control the expansion valve in response to determining an increase in the heat recovery load.
11. The refrigeration system of claim 10 , wherein the controller is configured to operate in the heat recovery mode of the plurality of heat recovery modes based at least in part on calculating an amount of heat transferred from the refrigerant to the process fluid through the heat recovery heat exchanger as a percentage of a value for an amount of heat transferred from the cooling fluid to the refrigerant in the evaporator added to an amount of power input to the compressor.
12. The refrigeration system of claim 11 , wherein the controller is configured to operate in a low heat recovery mode of the plurality of heat recovery modes when the calculated percentage is between 0 and a first threshold percentage greater than 0 percent, operate in an intermediate heat recovery mode of the plurality of heat recovery modes when the calculated percentage is between the first threshold percentage and a second threshold percentage greater than the first threshold percentage and less than 100 percent, and operate in a full heat recovery mode of the plurality of heat recovery modes when the calculated percentage is above the second threshold percentage.
13. The refrigeration system of claim 10 , wherein the economizer comprises:
a flash tank configured to at least partially vaporize the refrigerant; or
a heat exchanger configured to cool a first stream of the refrigerant by vaporizing a second stream of the refrigerant.
14. The refrigeration system of claim 10 , wherein the evaporator comprises:
a shell and tube evaporator, wherein the refrigerant flows through a shell side of the evaporator;
a shell and tube evaporator, wherein the refrigerant flows through a tube side of the evaporator; or
a plate heat exchanger, wherein the refrigerant flows in channels formed by plates.
15. A method, comprising:
determining if there is a demand for heat recovery through a heat recovery heat exchanger in a refrigeration system based on a set point temperature and a measured temperature of a process fluid exiting the heat recovery heat exchanger;
determining a heat recovery load in response to determining that there is the demand for heat recovery, wherein the heat recovery load is determined by comparing a determined amount of heat transferred from the refrigerant to the process fluid through the heat recovery heat exchanger with an amount of heat available from the refrigerant flowing through the refrigeration system; and
increasing a flow of the process fluid through the heat recovery heat exchanger, decreasing a fan speed of a condenser of the refrigeration system, and controlling an expansion valve of the refrigeration system in response to determining an increase in the heat recovery load.
16. The method of claim 15 , comprising:
controlling the refrigeration system based on a low heat recovery mode when the determined heat recovery load is a low heat recovery load;
controlling the refrigeration system based on an intermediate heat recovery mode when the determined heat recovery load is an intermediate heat recovery load; and
controlling the refrigeration system based on a full heat recovery mode when the determined heat recovery load is neither the low heat recovery mode nor the intermediate heat recovery load.
17. The method of claim 16 , wherein controlling the refrigeration system based on the low heat recovery mode comprises:
controlling the fan speed at a speed appropriate for normal chiller operation;
controlling the expansion valve to maintain a level of subcooling of the refrigerant exiting the condenser; and
maintaining a bypass valve to control flow of the process fluid through the heat recovery heat exchanger.
18. The method of claim 16 , wherein controlling the refrigeration system based on the intermediate heat recovery mode comprises:
calculating a first fan speed of the condenser based on normal chiller operation;
calculating a second fan speed of the condenser based on a temperature at a process fluid exit of the heat recovery heat exchanger;
driving a fan motor of the condenser at a minimum of the first and second fan speeds;
calculating a first valve opening of the expansion valve based on an amount of subcooling of refrigerant leaving the condenser;
calculating a second valve opening of the expansion valve based on an amount of subcooling of refrigerant leaving the heat recovery heat exchanger; and
opening the expansion valve to a maximum opening of the first and second valve openings.
19. The method of claim 16 , wherein controlling the refrigeration system based on the full heat recovery mode comprises:
controlling the fan speed at a speed calculated based on a temperature at a process fluid exit of the heat recovery heat exchanger;
controlling the expansion valve to maintain a level of subcooling of the refrigerant exiting the heat recovery heat exchanger; and
maintaining a bypass valve to initially open to allow full flow of the process fluid through the heat recovery heat exchanger.
20. The method of claim 15 , wherein determining the heat recovery load comprises calculating the amount of heat transferred from the refrigerant to the process fluid as a percentage of a value for an amount of heat transferred from a cooling fluid to the refrigerant in an evaporator of the refrigeration system added to an amount of power input to a compressor of the refrigeration system.
21. The method of claim 20 , comprising:
determining a low heat recovery load when the calculated percentage is between 0 and a first threshold percentage greater than 0 percent; and
determining an intermediate heat recovery load when the calculated percentage is between the first threshold percentage and a second threshold percentage less than 100 percent.
22. The refrigeration system of claim 1 , wherein the controller is configured to decrease the flow of the process fluid through the heat recovery heat exchanger, increase the fan speed of the condenser, and control the expansion valve in response to determining a decrease in the heat recovery load.