ECONOMIZED DEVICE CONTROL FOR REFRIGERATION SYSTEMS
Methods and systems for operating a refrigeration unit are provided. The methods and systems include measuring a first characteristic of a refrigeration unit, calculating a compressor middle stage pressure based on the first measured characteristic, determining if a first comparison and a second comparison are satisfied based on the first measured characteristic and the calculated compressor middle stage pressure, and opening an economizer solenoid valve when the first comparison and the second comparison are satisfied.
The subject matter disclosed herein generally relates to refrigeration systems and, more particularly, economized device control for refrigeration systems.
A particular difficulty of transporting perishable items is that such items must be maintained within a temperature range to reduce or prevent, depending on the items, spoilage, or conversely damage from freezing. A transport refrigeration unit is used to maintain proper temperatures within a transport cargo space. The transport refrigeration unit can be under the direction of a controller. The controller ensures that the transport refrigeration unit maintains a certain environment (e.g., thermal environment) within the transport cargo space.
SUMMARYAccording to one embodiment, a method for operating a refrigeration unit is provided. The method includes measuring a first characteristic of a refrigeration unit, calculating a compressor middle stage pressure based on the first measured characteristic, determining if a first comparison and a second comparison are satisfied based on the first measured characteristic and the calculated compressor middle stage pressure, and opening an economizer solenoid valve when the first comparison and the second comparison are satisfied.
In addition to one or more of the features described above, or as an alternative, further embodiments of the method may include that the first characteristic comprises a plurality of characteristics.
In addition to one or more of the features described above, or as an alternative, further embodiments of the method may include that the first characteristic comprises a flash tank pressure, a compressor suction pressure, and a discharge port pressure.
In addition to one or more of the features described above, or as an alternative, further embodiments of the method may include that the compressor middle stage pressure is calculated based on the compressor suction pressure and the discharge port pressure as Pmid=k1×(Psuc×Pdis)k
In addition to one or more of the features described above, or as an alternative, further embodiments of the method may include that the first characteristic comprises a flash tank pressure, the first comparison comprises comparing the calculated compressor middle stage pressure with a critical pressure modified by a first pressure constant, and the second comparison comprises comparing the flash tank pressure with the critical pressure.
In addition to one or more of the features described above, or as an alternative, further embodiments of the method may include monitoring a second characteristic, determining if a third comparison or a fourth comparison are satisfied based on the second characteristic, and closing the economizer solenoid valve when either the third comparison or the second comparison are satisfied.
In addition to one or more of the features described above, or as an alternative, further embodiments of the method may include that the second characteristic is at least one of (i) a time that a flash tank pressure exceeds a critical pressure modified by a first pressure constant and (ii) the flash tank pressure.
In addition to one or more of the features described above, or as an alternative, further embodiments of the method may include that the third comparison is satisfied if the time that the flash tank pressure exceeds the critical pressure modified by the first pressure constant exceeds a predetermined time.
In addition to one or more of the features described above, or as an alternative, further embodiments of the method may include that the fourth comparison is satisfied if the flash tank pressure exceeds the critical pressure modified by a second pressure constant.
In addition to one or more of the features described above, or as an alternative, further embodiments of the method may include, after closing the economizer solenoid valve, determining if the economizer solenoid valve should be opened again.
According to another embodiment, a refrigeration unit is provided. The refrigeration unit includes at least one sensor configured to measure a first characteristic of the refrigeration unit, a controller configured to calculate a compressor middle stage pressure based on the first characteristic the controller further configured to determine if a first comparison and a second comparison is satisfied based on the first characteristic and the calculated compressor middle stage pressure, and an economizer solenoid valve configured to open when the first comparison and the second comparison are satisfied.
In addition to one or more of the features described above, or as an alternative, further embodiments of the refrigeration unit may include that the first characteristic comprises a plurality of characteristics.
In addition to one or more of the features described above, or as an alternative, further embodiments of the refrigeration unit may include a flash tank, wherein the first characteristic comprises a flash tank pressure, a compressor suction pressure, and a discharge port pressure.
In addition to one or more of the features described above, or as an alternative, further embodiments of the refrigeration unit may include that the compressor middle stage pressure is calculated based on the compressor suction pressure and the discharge port pressure as Pmid=k1×(Psuc×Pdis)k
In addition to one or more of the features described above, or as an alternative, further embodiments of the refrigeration unit may include a flash tank, wherein the first characteristic comprises a flash tank pressure, the first comparison comprises comparing the calculated compressor middle stage pressure with a critical pressure modified by a first pressure constant, and the second comparison comprises comparing the flash tank pressure with the critical pressure.
In addition to one or more of the features described above, or as an alternative, further embodiments of the refrigeration unit may include that the controller is configured to determine if a third comparison or a fourth comparison are satisfied and wherein the economizer solenoid valve is configured to close when either the third comparison or the second comparison are satisfied.
In addition to one or more of the features described above, or as an alternative, further embodiments of the refrigeration unit may include that the controller is configured to monitor a second characteristic, wherein the second characteristic is at least one of (i) a time that a flash tank pressure exceeds a critical pressure modified by a first pressure constant and (ii) the flash tank pressure
In addition to one or more of the features described above, or as an alternative, further embodiments of the refrigeration unit may include that the third comparison is satisfied if the time that the flash tank pressure exceeds the critical pressure modified by the first pressure constant exceeds a predetermined time.
In addition to one or more of the features described above, or as an alternative, further embodiments of the refrigeration unit may include that the fourth comparison is satisfied if the flash tank pressure exceeds the critical pressure modified by a second pressure constant.
In addition to one or more of the features described above, or as an alternative, further embodiments of the refrigeration unit may include that the controller is further configured to determine if the economizer solenoid valve should be opened again after the economizer solenoid valve is closed.
Technical effects of embodiments of the present disclosure include a method of controlling a refrigeration unit to improve use of an economized mode of the refrigeration unit. Further technical effects include a refrigeration unit configured to improve use of an economized mode of the refrigeration unit. Further technical effects include calculating a compressor middle stage pressure and using such calculated compressor middle stage pressure to determine when to operate a refrigeration unit in an economized mode.
The foregoing features and elements may be combined in various combinations without exclusivity, unless expressly indicated otherwise. These features and elements as well as the operation thereof will become more apparent in light of the following description and the accompanying drawings. It should be understood, however, that the following description and drawings are intended to be illustrative and explanatory in nature and non-limiting.
The subject matter is particularly pointed out and distinctly claimed at the conclusion of the specification. The foregoing and other features, and advantages of the present disclosure are apparent from the following detailed description taken in conjunction with the accompanying drawings in which:
As shown and described herein, various features of the disclosure will be presented. Various embodiments may have the same or similar features and thus the same or similar features may be labeled with the same reference numeral, but preceded by a different first number indicating the figure to which the feature is shown. Thus, for example, element “a” that is shown in FIG. X may be labeled “Xa” and a similar feature in FIG. Z may be labeled “Za.” Although similar reference numbers may be used in a generic sense, various embodiments will be described and various features may include changes, alterations, modifications, etc. as will be appreciated by those of skill in the art, whether explicitly described or otherwise would be appreciated by those of skill in the art.
Shown in
Referring now to
Airflow is circulated into and through the cargo compartment of the trailer 106 by means of the refrigeration unit 120. A return airflow 134 flows into the refrigeration unit 120 from the cargo compartment of the trailer 106 through a refrigeration unit inlet 136, and across the evaporator 128 via the evaporator fan 130, thus cooling the return airflow 134 to a selected or predetermined temperature. The cooled return airflow 134, now referred to as supply airflow 138, is supplied into the cargo compartment of the trailer 106 through a refrigeration unit outlet 140, which in some embodiments is located near the top wall 108 of the trailer 106. The supply airflow 138 cools the cargo 118 in the cargo compartment of the trailer 106. It is to be appreciated that the refrigeration unit 120 can further be operated in reverse to warm the trailer 106 when, for example, the outside temperature is very low.
The refrigeration unit 120 is positioned in a frame 142 and contained in an accessible housing 144, with the frame 142 and/or the housing 144 secured to an exterior side of the front wall 114 such that the refrigeration unit 120 is positioned between the front wall 114 and the tractor 102, as shown in
It will be appreciated by those of skill in the art that the systems and configurations of
Turning now to
In operation, high temperature, high pressure refrigerant vapor exiting the compressor 222 is directed to a condenser 224, which can include a plurality of condenser coil fins and tubes, which receive air, typically blown by a condenser fan. As shown, the condenser 224 may include an intercooler 223 and a gas cooler 225. By removing heat through the condenser 224, the refrigerant changes to a high pressure/lower temperature state.
The refrigerant may flow from the gas cooler 225 of the condenser 224 to a flash tank 246. A high pressure expansion device 248 may be located between the gas cooler 225 and the flash tank 246. The flash tank 246 may be fluidly connected to an evaporator 228 and to a portion of the compressor 222. An electronic evaporator expansion valve 250 may be located between the flash tank 246 and the evaporator 228. The refrigerant may then flow from the evaporator 228 back to the compressor 222, to form a complete refrigerant circuit.
As shown and noted above, the compressor 222 may be a multi-stage compressor. As shown in
Many of the points in the refrigeration unit 220 can be monitored and controlled by a controller 260 and various associated sensors (not shown) located throughout the refrigeration unit 220. The controller 260 can include a microprocessor and an associated memory. The memory of controller 260 can contain operator and/or owner preselected, desired values for various operating parameters within the refrigeration unit 220 including, but not limited to, temperature set points for various locations within the refrigeration unit 220, pressure limits, current limits, engine speed limits, and any variety of other desired operating parameters or limits with the refrigeration unit 220. In one embodiment, the controller 260 can include a microprocessor board that contains a microprocessor and memory, an input/output (I/O) board that can include an analog to digital converter. The I/O board can receive temperature inputs and pressure inputs from various points in the system, i.e. from the various sensors, AC current inputs, DC current inputs, voltage inputs and humidity level inputs. In addition, the I/O board can include drive circuits or field effect transistors (“FETs”) and relays to receive signals or current from the controller 260 and in turn control various external or peripheral devices in the refrigeration unit 220.
Among exemplary sensors and/or transducers monitored by controller 260 can be a return air temperature sensor that inputs into the controller 260 a variable resistor value according to the evaporator return air temperature. An ambient air temperature sensor that can provide the controller 260 an ambient air temperature value (e.g., detected in front of or upstream of the condenser 224). A compressor suction temperature sensor that can input to the controller 260 a variable resistor value according to a compressor suction temperature. A compressor discharge temperature sensor that can detect a compressor discharge temperature inside the compressor 222. An evaporator outlet temperature sensor and an evaporator outlet pressure transducer that can detect an outlet temperature value and an evaporator outlet pressure of evaporator 228. A compressor suction pressure transducer can provide the controller 260 a variable voltage according to a compressor suction value of the compressor 222. A compressor discharge pressure transducer that can provide to the controller 260 a variable voltage according to a compressor discharge value of compressor 222. In addition, a direct current sensor and an alternating current sensor can detect current drawn by the compressor 222. A sensor may be configured to read a pressure on the flash tank 246.
One function of the controller 260 may be to control, e.g., open and/or close the economizer solenoid valve 258. The controller 260 may control the economizer solenoid valve 258 to ensure the refrigeration unit 220 operates in an economized mode whenever possible in order to gain increased capacity and efficiency from the refrigeration unit 220. One solution to ensure optimized economized mode operation is to apply dedicated and specific switch logic to force the system into economized mode by opening the economizer solenoid valve 258; however this solution may create the risk of injecting high density refrigerant into the compressor 222, which may be detrimental to the components of the system.
In some refrigeration systems, two conditions may exist to enable the system to run in the economized mode. The two conditions are (i) compressor middle stage pressure should be below the critical pressure of the refrigerant, and (ii) the high pressure expansion device 248 and the electronic evaporator expansion valve 250 are capable to maintain the pressure in the flash tank 246 at a pressure equal to a pressure in the economizer line 256. Based on these two conditions, embodiments described herein provide an economizer solenoid valve, such as an economized solenoid valve, control process. The control process includes taking measurement of various pressures within the system, calculating or predicting a compressor middle stage pressure, and defining criteria to determine the economized solenoid valve to be open or closed—and thus operate in the economized mode.
Turning now to
At the beginning of the flow process 300, an economizer solenoid valve may be in a closed state at block 302. In operation, one or more readings or measurements may be taken within the refrigeration unit at block 304. For example, the pressure within a flash tank Pft, a compressor suction pressure Psuc, and a pressure at a discharge port Pdis may be measured. The values may be conveyed to or read by a processor or other control device or controller.
The controller may then predict a pressure at a middle stage of the compressor Pmid at block 306. The middle stage pressure Pmid may be based on the compressor suction pressure Psuc and the discharge pressure Pdis. The calculation may be based, in part, on the design and configuration of the refrigeration unit, and may in some embodiments, be based on the design and/or configuration of the compressor. For example, in a non-limiting embodiment, given a number of constants and/or known parameters (e.g., k1, k2, k3), the middle stage pressure Pmid may be calculated with the following equation: Pmid=k1×(Psuc×Pdis)k
Next, the controller may make comparisons of the various known/calculated values to determine if the refrigeration unit should be operated in an economized mode at block 308. For example, the calculated middle stage pressure Pmid may be compared to a known and/or predetermined value that is configured to enable operation of the refrigeration unit in an economized mode. Further, the flash tank pressure Pft may be compared to a known and/or predetermined value.
For example, as shown at block 308 of
As such, when it is determined that both the first comparison C1 and the second comparison C2 are satisfied, the flow process 300 will continue to block 310 and the economizer solenoid valve will be opened. As shown, the economizer solenoid valve is referred to as an economized solenoid valve, but those of skill in the art will appreciate that other economizer solenoid valves may be used without departing from the scope of the present disclosure.
Next, at block 312, if the economizer solenoid valve is open for a period wherein if the flash tank pressure Pft is greater than a predetermined value, the economizer solenoid valve will be closed. Thus, at block 312, the controller will make the following comparisons: a third comparison C3: t[Pft>(Pcrit−dP1)]>t1 and a fourth comparison C4: Pft>(Pcrit+dP2).
In the third comparison C3, the controller is tracking the time that the flash tank pressure Pft is greater than a pressure valve based on the critical pressure of the refrigerant Pcrit and comparing it against the predetermined time t1. In the fourth comparison C4, the controller is monitoring the flash tank pressure Pft and ensuring that the pressure in the flash tank Pft does not exceed a pressure value based on the critical pressure of the refrigerant Pcrit as modified with a second pressure constant dP2.
If it is determined that neither the third comparison C3 nor the fourth comparison C4 is satisfied, the economized mode will be maintained and the economizer solenoid valve will remain open. However, if it is determined that either of the third comparison C3 or the fourth comparison C4 are satisfied, the process 300 will continue to block 314 and the economizer solenoid valve will be closed. Once the economizer solenoid valve is closed and the economized mode is exited, the process 300 will begin again at block 302 and the pressures Pft, Psuc, and Pdis will be measured and the middle stage pressure Pmid will be calculated (blocks 304, 306) and the values will be compared in the first comparison C1 and the second comparison C2 at block 308.
Advantageously, embodiments described herein provide a refrigeration unit having an improved economized mode operation and/or use. For example, advantageously in accordance with various embodiments, an improved economized solenoid valve control is provided by introducing a predicted or calculated compressor middle stage pressure into criteria for determining when to open or close an economizer solenoid valve. The economizer solenoid valve control as provided herein allows the system to operate in an economized mode when it should, and further eliminates the use of special switch logic. Further, advantageously, embodiments described herein avoid the risk of damaging the compressor of a refrigeration unit. Moreover, embodiments provided herein may ensure that a refrigeration unit or system will operate with optimized capacity and/or efficiency.
While the present disclosure has been described in detail in connection with only a limited number of embodiments, it should be readily understood that the present disclosure is not limited to such disclosed embodiments. Rather, the present disclosure can be modified to incorporate any number of variations, alterations, substitutions, combinations, sub-combinations, or equivalent arrangements not heretofore described, but which are commensurate with the scope of the present disclosure. Additionally, while various embodiments of the present disclosure have been described, it is to be understood that aspects of the present disclosure may include only some of the described embodiments.
For example, although various embodiments described herein include specific components and/or arrangements of components, other components and/or substitutions thereof may be employed without departing from the scope of the present disclosure. Further, although a process is described herein with a specific order of steps, those of skill in the art will appreciate that the process may include additional and/or alternative steps and further the steps may be performed in any order and/or simultaneously, without departing from the scope of the present disclosure.
Accordingly, the present disclosure is not to be seen as limited by the foregoing description, but is only limited by the scope of the appended claims.
Claims
1. A method for operating a refrigeration unit, the method comprising:
- measuring a first characteristic of a refrigeration unit;
- calculating a compressor middle stage pressure based on the first measured characteristic;
- determining if a first comparison and a second comparison are satisfied based on the first measured characteristic and the calculated compressor middle stage pressure; and
- opening an economizer solenoid valve when the first comparison and the second comparison are satisfied.
2. The method of claim 1, wherein the first characteristic comprises a plurality of characteristics.
3. The method of claim 2, wherein the first characteristic comprises a flash tank pressure, a compressor suction pressure, and a discharge port pressure.
4. The method of claim 3, wherein the compressor middle stage pressure is calculated based on the compressor suction pressure and the discharge port pressure as Pmid=k1×(Psuc×Pdis)k2+k3, wherein k1, k2, k3 are known parameters.
5. The method of claim 1, wherein the first characteristic comprises a flash tank pressure, the first comparison comprises comparing the calculated compressor middle stage pressure with a critical pressure modified by a first pressure constant, and the second comparison comprises comparing the flash tank pressure with the critical pressure.
6. The method of claim 1, further comprising:
- monitoring a second characteristic;
- determining if a third comparison or a fourth comparison are satisfied based on the second characteristic; and
- closing the economizer solenoid valve when either the third comparison or the second comparison are satisfied.
7. The method of claim 6, wherein the second characteristic is at least one of (i) a time that a flash tank pressure exceeds a critical pressure modified by a first pressure constant and (ii) the flash tank pressure.
8. The method of claim 7, wherein the third comparison is satisfied if the time that the flash tank pressure exceeds the critical pressure modified by the first pressure constant exceeds a predetermined time.
9. The method of claim 7, wherein the fourth comparison is satisfied if the flash tank pressure exceeds the critical pressure modified by a second pressure constant.
10. The method of claim 6, further comprising, after closing the economizer solenoid valve, determining if the economizer solenoid valve should be opened again.
11. A refrigeration unit comprising:
- at least one sensor configured to measure a first characteristic of the refrigeration unit;
- a controller configured to calculate a compressor middle stage pressure based on the first characteristic the controller further configured to determine if a first comparison and a second comparison is satisfied based on the first characteristic and the calculated compressor middle stage pressure; and
- an economizer solenoid valve configured to open when the first comparison and the second comparison are satisfied.
12. The refrigeration unit of claim 11, wherein the first characteristic comprises a plurality of characteristics.
13. The refrigeration unit of claim 12, further comprising a flash tank, wherein the first characteristic comprises a flash tank pressure, a compressor suction pressure, and a discharge port pressure.
14. The refrigeration unit of claim 13, wherein the compressor middle stage pressure is calculated based on the compressor suction pressure and the discharge port pressure as Pmid=k1×(Psuc×Pdis)k2+k3, wherein k1, k2, k3 are known parameters.
15. The refrigeration unit of claim 11, further comprising a flash tank, wherein the first characteristic comprises a flash tank pressure, the first comparison comprises comparing the calculated compressor middle stage pressure with a critical pressure modified by a first pressure constant, and the second comparison comprises comparing the flash tank pressure with the critical pressure.
16. The refrigeration unit of claim 11, wherein the controller is configured to determine if a third comparison or a fourth comparison are satisfied and wherein the economizer solenoid valve is configured to close when either the third comparison or the second comparison are satisfied.
17. The refrigeration unit of claim 16, wherein the controller is configured to monitor a second characteristic, wherein the second characteristic is at least one of (i) a time that a flash tank pressure exceeds a critical pressure modified by a first pressure constant and (ii) the flash tank pressure
18. The refrigeration unit of claim 17, wherein the third comparison is satisfied if the time that the flash tank pressure exceeds the critical pressure modified by the first pressure constant exceeds a predetermined time.
19. The refrigeration unit of claim 17, wherein the fourth comparison is satisfied if the flash tank pressure exceeds the critical pressure modified by a second pressure constant.
20. The refrigeration unit of claim 16, wherein the controller is further configured to determine if the economizer solenoid valve should be opened again after the economizer solenoid valve is closed.
Type: Application
Filed: Nov 16, 2016
Publication Date: Aug 13, 2020
Inventors: Jian Sun (Fayetteville, NY), Mark J. Perkovich (Fayetteville, NY)
Application Number: 15/776,153