Patent Application
20050132735
The present invention relates generally to a system and method of optimizing a transcritical vapor compression system by maximizing the system heating capacity.
Chlorine containing refrigerants have been phased out in most of the world due to their ozone destroying potential. Hydrofluorocarbons (HFCs) have been used as replacement refrigerants, but these refrigerants still have high global warming potential.
“Natural” refrigerants, such as carbon dioxide and propane, have been proposed as replacement fluids. Carbon dioxide can be used as a refrigerant in automotive air conditioning systems and other heating and cooling applications. Carbon dioxide has a low critical point, which causes most air conditioning systems utilizing carbon dioxide as a refrigerant to run transcritically, or partially above the critical point, under most conditions.
A vapor compression system must be able to provide enough heating capacity to meet the load requirements during the winter when the outdoor air temperature is the lowest. For a given set of operating conditions, there is a high side pressure value which maximizes the coefficient of performance. A different high side pressure value for the same set of operating conditions maximizes the heating capacity. The high side pressure is generally selected to optimize the coefficient of performance. The coefficient of performance is very sensitive to the high side pressure when the high side pressure of the system is set below the high side pressure that optimizes the coefficient of performance. However, the coefficient of performance becomes insensitive to the high side pressure when the high side pressure of the system is set above the optimal high side pressure.
In prior vapor compressions systems, the vapor compression system is oversized to achieve sufficient heating capacity in low ambient conditions. A drawback to oversizing a vapor compression system is that it is expensive and requires more space.
Hence, there is a need in the art for a system and method of optimizing the heating capacity of a vapor compression system as well as overcoming the disadvantages of the prior art.
A transcritical vapor compression system includes a compressor, a gas cooler, an expansion device, and an evaporator. Refrigerant is circulated though the closed circuit cycle. In one example, the refrigerant is carbon dioxide. Carbon dioxide has a low critical point, and systems utilizing carbon dioxide as the refrigerant usually operate transcritically. In the present invention, high pressure of the vapor compression system is regulated to optimize the heating capacity of the system.
In one example system, the optimal heating capacity of the vapor compression system is determined by measuring the current required to operate the water pump that pumps water through the gas cooler to accept heat from the refrigerant. The higher the current required to operate the water pump, the higher the flowrate of the water through the gas cooler, and the higher the heat exchange between the water and the refrigerant in the gas cooler. That is, the higher the current to operate the water pump, the higher the heating capacity of the system. At a given high side pressure, the heating capacity is calculated based upon the measured current required to operate the heat pump. The high side pressure of the system is continually adjusted and current readings of the heat pump are obtained until the maximum current, and therefore optimal heating capacity, is obtained.
In another example system, the heating capacity of the vapor compression system is maximized by regulating the high side pressure based upon several measured system characteristics. The ambient air temperature, the inlet temperature of the heat sink of the gas cooler and the outlet temperature of the heat sink of the gas cooler are measured. A controller then correlates the measured temperatures to a pre-determined high pressure side programmed in the controller that obtains the optimal heating capacity for the given operating conditions. Based on this analysis, the controller adjusts the orifice of the expansion device to regulate the high side pressure in the system to achieve the pre-determined optimal heating capacity.
These and other features of the present invention will be best understood from the following specification and drawings.
The various features and advantages of the invention will become apparent to those skilled in the art from the following detailed description of the currently preferred embodiment. The drawings that accompany the detailed description can be briefly described as follows:
The refrigerant exits the compressor 22 at a high pressure and a high enthalpy. The refrigerant then flows through the gas cooler 24 at a high pressure. A fluid medium 30, such as water or air, flows through a heat sink 32 of the gas cooler 24 and exchanges heat with the refrigerant flowing through the gas cooler 24. In the gas cooler 24, the refrigerant rejects heat into the fluid medium 30, and the refrigerant exits the gas cooler 24 at a low enthalpy and a high pressure. A water pump 34 pumps the fluid medium through the heat sink 32. The cooled fluid medium 30 enters the heat sink 32 at the heat sink inlet or return 36 and flows in a direction opposite to or cross to the direction of the flow of the refrigerant. After exchanging heat with the refrigerant, the heated water 38 exits the heat sink 30 at the heat sink outlet or supply 40.
The refrigerant then passes through the expansion device 26, which regulates the pressure of the refrigerant. The expansion device 26 can be an electronic expansion valve (EXV) or other known type of expansion device.
After passing through the expansion valve, the refrigerant flows through the passages 70 of the evaporator 28 and exits at a high enthalpy and a low pressure. In the evaporator 28, the refrigerant absorbs heat from a heated fluid medium 44, heating the refrigerant. In one example, the heated fluid medium 44 is outdoor air. The heated fluid medium 44 flows through a heat sink 46 and exchanges heat with the refrigerant passing through the evaporator 28 in a known manner. The heated fluid medium 44 enters the heat sink 46 through the heat sink inlet or return 48 and flows in a direction opposite or cross to the direction of flow of the refrigerant. After exchanging heat with the refrigerant, the cooled fluid medium 50 exits the heat sink 46 through the heat sink outlet or supply 52. The temperature difference between the heated fluid medium 44 and the refrigerant in the evaporator 28 drives the thermal energy transfer from the heated fluid medium 44 to the refrigerant as the refrigerant flows through the evaporator 28. A fan 54 moves the heated fluid medium 44 across the evaporator 28, maintaining the temperature difference and evaporating the refrigerant. The refrigerant then reenters the compressor 22, completing the cycle.
The system 20 transfers heat from the low temperature energy reservoir (ambient air) to the high temperature energy sink (heated hot water). The transfer of energy is also achieved with the aid of electrical energy input at the compressor 22.
The system 20 can also include an accumulator 56. The accumulator 56 stores excess refrigerant from the system 20.
In one example, carbon dioxide is used as the refrigerant. Although carbon dioxide is described, other refrigerants may be used. Because carbon dioxide has a low critical point, systems utilizing carbon dioxide as a refrigerant usually run transcritically.
The heating capacity of a vapor compression system 20 is defined as the capacity of the system 20 to heat the water 30 that flows through the gas cooler 24 and accepts heat from the refrigerant flowing through the gas cooler 24. A vapor compression system 20 usually operates under a wide range of operating conditions. For example, the temperature of the outdoor air 44 can vary between −10° F. in the winter and 120° F. in the summer, which can cause the temperature of the refrigerant exiting the evaporator 28 to vary between approximately −20° F. and 90° F. Therefore, the heating capacity of the vapor compression system 20 in the summer is generally four to five times greater than the heating capacity of the vapor compression system 20 in the winter, and the refrigerant mass flow rate of the vapor compression system 20 in the summer is generally eight to ten times greater than the refrigerant mass flow rate of the vapor compression system 20 in the winter. Although the heating capacity of the vapor compression system 20 changes as operating conditions change, the heating load required of the vapor compression system 20 does not change as the ambient temperature change.
As the high side pressure increases to P1, both the heating capacity and the coefficient of performance increase significantly. At P1, the coefficient of performance is maximized. As the high side pressure increases from P1 to P2, the heating capacity continues to increase significantly while the coefficient of performance decreases only slightly. At P2, the heating capacity is optimized, but the coefficient of performance has only negligibly decreased.
In the present invention, the system 20 operates in an optimizing heating capacity mode when a sensor 60 (shown in
When the sensor 60 detects that the temperature of the fluid medium 44 is above the threshold value, the system 20 operates in a normal mode. That is, the system 20 operates to optimize the coefficient performance. When the sensor 60 detects that the temperature of the fluid medium 44 is below the threshold value, the system 20 operates in a heating capacity mode. When operating in the heating capacity mode, the heating capacity is optimized by determining the optimal system heating capacity pressure P2, measuring the actual system high side pressure PH, and then regulating the actual system high side pressure PH to the optimal system heating capacity pressure P2.
A controller 29 regulates the system 20. At a given high side pressure, the heating capacity can be calculated based on the current measured to operate the water pump 34. The controller 29 stores the calculated heating capacity value at the given high side pressure. The calculated heating capacity is compared to a stored value of system heating capacity. The high side pressure of the system 20 is continually changed until the current that operates the heat pump 34 is the greatest. When the maximum current is determined, the corresponding high side pressure is the pressure that optimizes the heating capacity. The system 20 is run at this high side pressure to maximize capacity.
For example, the high side pressure can be set to 1500 psi. At this high side pressure, the controller 29 detects that the heat pump 34 is using 10 milliamps of current. The high side pressure is then adjusted to at 1550 psi. The controller 29 then detects that the heat pump 34 is using 10.5 milliamps of current. The high side pressure is then adjusted to 1600 psi. The controller 29 then detects that the heat pump 34 is using 10.2 milliamps of current. In this example, the heat pump 34 uses the highest amount of current when system is operating at a high side pressure of 1550 psi. Therefore, at this high side pressure, the heating capacity of the system 20 is optimized.
Optimal high side pressure values for various temperatures are programmed and stored in the controller 29. Based on the detected temperatures, an optimal high side pressure is determined. Alternately, the optimal size or percentage of the orifice of the expansion device 26 is determined based on the detected temperatures. Alternately, the control current for the expansion valve 26 is determined based on the detected temperatures.
The actual system high side pressure PH is then regulated to achieve the optimal system heating capacity pressure P2. The actual system high side pressure PH can be regulated by adjusting an orifice 58 of the expansion device 26. Opening the orifice 58 increases the flowrate of the refrigerant through the expansion device 26, causing more mass to leave the high pressure part of the system, decreasing the instantaneous refrigerant mass in the high pressure part of the system, and decreasing the system high side pressure PH. Closing the orifice decreases the flowrate of the refrigerant through the expansion device 26, causing less mass to leave the high pressure part of the system, increasing the instantaneous refrigerant mass in the high pressure part of the system, and increasing the system high side pressure PH. The system high side pressure PH can be regulated in other ways, and one skilled in the art would know how to regulate the high side pressure.
The foregoing description is only exemplary of the principles of the invention. Many modifications and variations of the present invention are possible in light of the above teachings. The preferred embodiments of this invention have been disclosed, however, so that one of ordinary skill in the art would recognize that certain modifications would come within the scope of this invention. It is, therefore, to be understood that within the scope of the appended claims, the invention may be practiced otherwise than as specifically described. For that reason the following claims should be studied to determine the true scope and content of this invention.
