The present invention relates to refrigeration systems and, more particularly, to fluid defrost of heat exchangers in refrigeration systems.
Refrigeration systems are well known and widely used in supermarkets, warehouses, and elsewhere to refrigerate product that is supported in a refrigerated space. Conventional refrigeration systems include a heat exchanger or evaporator, a compressor, and a condenser. The evaporator provides heat transfer between a refrigerant flowing within the evaporator and a fluid (e.g., water, air, etc.) passing over or through the evaporator. The evaporator transfers heat from the fluid to the refrigerant to cool the fluid. The refrigerant absorbs the heat from the fluid and evaporates in a refrigeration mode, during which the compressor mechanically compresses the evaporated refrigerant from the evaporator and feeds the superheated refrigerant to the condenser, which cools the refrigerant. From the condenser, the cooled refrigerant is typically fed through an expansion valve to reduce the temperature and pressure of the refrigerant, and then the refrigerant is directed through the evaporator.
Some evaporators operate at evaporating refrigerant temperatures that are near or lower than the freezing point of water (i.e., 32 degrees Fahrenheit). Over time, water vapor from the fluid freezes on the evaporator (e.g., on the coils) and generates frost. Accumulation of frost decreases the efficiency of heat transfer between the evaporator and the fluid passing over the evaporator, which causes the temperature of the refrigerated space to increase above a desired level. Maintaining the correct temperature of the refrigerated space is important to maintain the quality of the stored product. To do this, evaporators must be regularly defrosted to reestablish efficiency and proper operation. Many existing refrigeration systems use electric heaters that are placed underneath the evaporator to defrost the evaporator using convection heat. Other existing systems re-route hot gaseous refrigerant from the compressor directly to the evaporator so that heat from the hot refrigerant melts the frost on the evaporator (i.e. reverse hot gas defrost). Some evaporators draw air through a coil of the evaporator, which creates turbulent airflow through the coil. The turbulent airflow is further intensified with higher volumes of air, common in commercial refrigeration units. Many existing refrigeration systems include a sensor to measure a pressure differential within the coil. However, a pressure differential within the coil is generally higher than the pressure differential in the remainder of the refrigeration system due to the turbulent airflow within coil. In addition, the sensors are typically located within the volume or envelope of the coil, which reduces the capacity of the evaporator to condition the airflow because fins of the evaporator need to be adjusted or trimmed. Trimming the fins has a negative impact on coil performance.
Frost and ice that forms on an evaporator of a commercial refrigeration system, such as a refrigerated merchandiser, acts as an insulating barrier that reduces heat transfer and can lead to reduced airflow across the coil. The rate of frost accumulation can vary significantly depending on variables such as ambient conditions, shopping volume, and/or case maintenance. Demand defrost, embodying the invention as described herein, initiates defrost cycles only when there is sufficient frost accumulation (as detected by appropriate mechanisms), which reduces overall energy usage and improves average product temperatures.
In one aspect, the present invention provides a refrigeration system having a refrigerant circuit including a condenser, an evaporator, a compressor, and a control system. The compressor is configured to circulate a cooling fluid through the refrigerant circuit. The refrigerant circuit has an inlet line fluidly connecting the condenser to the evaporator and a suction line fluidly connecting the evaporator to the compressor. The control system begins a defrost cycle for the refrigeration system based on a differential pressure of the evaporator.
Other aspects of the invention will become apparent by consideration of the detailed description and accompanying drawings.
Before any embodiments of the invention are explained in detail, it is to be understood that the invention is not limited in its application to the details of construction and the arrangement of components set forth in the following description or illustrated in the following drawings. The invention is capable of other embodiments and of being practiced or of being carried out in various ways. Also, it is to be understood that the phraseology and terminology used herein is for the purpose of description and should not be regarded as limiting.
Features illustrated or described as part of one embodiment can be used with another embodiment to yield a still further embodiment. Thus, it is intended that the present invention covers such modifications and variations as come within the scope of the appended claims and their equivalents. The Detailed Description uses numerical and letter designations to refer to features in the drawings. Like or similar designations in the drawings and description have been used to refer to like or similar parts of the invention.
As used herein, the terms “first,” “second,” and “third” may be used interchangeably to distinguish one component from another and are not intended to signify location or importance of the individual components. The singular forms “a,” “an,” and “the” include plural references unless the context clearly dictates otherwise. The terms “coupled,” “fixed,” “attached to,” and the like refer to both direct coupling, fixing, or attaching, as well as indirect coupling, fixing, or attaching through one or more intermediate components or features, unless otherwise specified herein. As used herein, the terms “comprises,” “comprising,” “includes,” “including,” “has,” “having” or any other variation thereof, are intended to cover a non-exclusive inclusion. For example, a process, method, article, or apparatus that comprises a list of features is not necessarily limited only to those features but may include other features not expressly listed or inherent to such process, method, article, or apparatus. Further, unless expressly stated to the contrary, “or” refers to an inclusive- or and not to an exclusive- or. For example, a condition A or B is satisfied by any one of the following: A is true (or present) and B is false (or not present), A is false (or not present) and B is true (or present), and both A and B are true (or present).
Terms of approximation, such as “generally,” “approximately,” or “substantially,” include values within ten percent greater or less than the stated value. When used in the context of an angle or direction, such terms include within ten degrees greater or less than the stated angle or direction. For example, “generally vertical” includes directions within ten degrees of vertical in any direction (e.g., clockwise or counterclockwise).
Benefits, other advantages, and solutions to problems are described below with regard to specific embodiments. However, the benefits, advantages, solutions to problems, and any feature(s) that may cause any benefit, advantage, or solution to occur or become more pronounced are not to be construed as a critical, required, or essential feature of any or all the claims.
As best shown in
The refrigeration system 45 has a refrigeration mode during which the evaporator 60 conditions an airflow (e.g., the air flowing through passageway 70 in the merchandiser 10) based on heat transfer between the refrigerant in the evaporator 60 and air passing over the evaporator 60 (i.e. the refrigerant takes on heat from the air passing over the evaporator 60). The refrigeration system also has a defrost mode during which frost buildup on the evaporator 60 is reduced or removed. Although the invention is described with reference to its application in the refrigerated merchandiser 10, it will be appreciated that the refrigeration system 45 and defrost control described in detail below may have other applications.
With reference to
The outlet tap 108 is disposed or located at the outlet 94 of the evaporator 60 to detect air pressure at or adjacent the outlet 94. The ambient tap 112 is disposed on or located at or adjacent an external surface of the refrigeration system 45 or otherwise positioned (e.g., in or on an electrical raceway, exterior of the raceway, on the canopy 30, on an exterior side of the base 20, etc.) so that the sensor 106 may detect ambient air pressure (e.g., via vacuum tubing with an ambient port). The sensor 106 obtains pressure readings or data from the outlet tap 108 and the ambient tap 112 and provides the pressure data to the control system 104 so that the control system 104 can determine whether to initiate or stop defrost based on the pressure data alone or in combination with one or more other factors (e.g., whether a door of the merchandiser 10 is open, time of day, etc.). The location of the outlet tap 108 is chosen so that the outlet tap 108 is situated to detect the static pressure drop across the evaporator 60 (e.g., relative to ambient pressure or inlet air pressure). In some embodiments, pressure differential may be measured based on the evaporator inlet pressure and the evaporator outlet pressure. The ambient tap is open to atmosphere/outside the merchandiser in the electrical raceway, although it will be appreciated that the ambient tap 112 may be located elsewhere on the merchandiser 10 (e.g., the canopy 30, etc.).
The ambient tap 112 is located externally of components of the refrigeration system 45 and is open to atmosphere (e.g., external to the merchandiser 10, or external to the airflow envelope of the merchandiser 10) 45 to measure the pressure of ambient air adjacent the merchandiser 10. In one non-limiting example, the control system 104 measures a pressure differential between the ambient air pressure measured by the ambient tap 112 and the air pressure measured by the outlet tap 108. In the illustrated example, when the pressure differential between the ambient tap 112 and the outlet tap 108 drops below a pressure trigger value (e.g., for a predetermined timeframe), the control system 104 initiates a defrost cycle. In another example, the sensor 106 may sample from an inlet tap 210 rather than, or in addition to, the ambient tap 112. The inlet tap 210 may be coupled to the sensor 106 via vacuum tubing such that the sensor 106 provides pressure readings or data from the inlet tap 210 to the control system 104. In these embodiments, the control system 104 may determine the pressure differential based on the pressure readings at the outlet tap 108 and the inlet tap 210. It will be appreciated that the ambient pressure and the outlet pressure may be sensed by a sensor or sensors other than vacuum tube sensor(s).
The control system 104 includes a controller 120 that is electrically connected to the sensor 106. The controller 120 continuously or periodically measures the pressure differential between the ambient tap 112 and the outlet tap 108. In some embodiments, the defrost cycle is initiated when the pressure differential drops below the pressure trigger value for a minimum time. In some embodiments, the minimum time interval may reset whenever the pressure differential rises above the pressure trigger value or when the door is opened. Therefore, in some embodiments, the pressure differential must be below the pressure trigger value for the entirety of the minimum time interval before defrost is initiated (and in some circumstances, without the door being opened). In other embodiments, the pressure differential may be below the pressure trigger value for less than the entirety of the minimum time while still triggering defrost. In some embodiments, the controller 120 may control defrost without determining that a door is open or disregard when the door is opened such that a door opening event does not reset the minimum time. A door opening event may be detected directly via a sensor (e.g., operatively in communication with the door), or using controller logic to determine that a door is opened based on a sudden pressure change (e.g., the differential pressure equalizes to ambient pressure for a brief period while the door is opened) relative to the running average for the pressure differential over a period of time (e.g., 30 minutes).
The controller 120 selectively initiates a demand defrost cycle (e.g., outside of one or more timeframes when defrost is prevented, such as during times of high traffic or use; referred to herein as a “refrigeration window”) when the current or detected differential pressure P drops below a pressure trigger value Pset for more than a minimum time Tmin. That is, the time Tcount that the pressure differential is below the pressure trigger value must reach or exceed the minimum time Tmin before the controller 120 initiates a demand defrost cycle. As described below, the controller 120 may account for additional information before initiating a demand defrost cycle. The minimum time Tmin may be reset whenever the differential pressure P is determined to be greater than the predetermined value Pset or after a defrost cycle. In some embodiments including the merchandiser 10 with a door, the minimum time Tmin may reset when the door is opened. After defrost, the controller 120 waits a minimum defrost wait time interval Tint before the controller 120 can initialize another demand defrost cycle. The minimum defrost wait time interval Tint for an open-front merchandiser 10 may be 4 hours, or more or less than 4 hours. The minimum defrost wait time interval Tint for a reach-in merchandiser 10 including doors 42 may be 24 hours, or more or less than 24 hours. It will be appreciated that the minimum defrost wait time interval Tint for may vary depending on humidity or tropical conditions, especially in environments that do not have building air conditioning systems. In the latter situation, defrost likely will be more frequent.
The pressure trigger value Pset is determined based on an initial pressure differential Pinitial, which is determined during or shortly after initialization of a merchandiser 10 as described below. The pressure trigger value Pset is a pressure differential value determined based on the pressure differential Pinitial and a multiplier (e.g., a percentage value) that is input into or stored in the controller 120 (e.g., Pset=Pinitial*i, where ‘i’ is a set trigger percentage). The pressure trigger value Pset, when determined to be substantially below the initial pressure differential Pinitial is indicative of one or more adverse conditions associated with the merchandiser 10 and, in particular, the refrigeration system 45. In some embodiments, the pressure trigger value may be a percentage value of the initial pressure differential. In non-limiting examples, the set trigger percentage may be 35-40%, lower than 50%, or 50-60%. It will be appreciated that the set trigger percentage may be other values.
With continued reference to
With reference to
In the defrost mode or defrost cycle, components of the refrigeration system 45 are heated to remove or reduce frost that has built up during the refrigeration mode. In the defrost cycle, the heater 75 is activated, which begins heating the refrigerant flowing to the evaporator 60. The flow control device 55 regulates (e.g., maintains, increases, or decreases) the flow of refrigerant to the evaporator 60 during the defrost mode, and ensures that refrigerant continues to flow to the evaporator 60 in the defrost mode. The pressure control apparatus 80 is configured to increase system pressure during the defrost mode to maintain flow of refrigerant into the evaporator 60 and to control flow of refrigerant to the compressor 65. Refrigerant continues to flow to the compressor 65 during the defrost mode. In general, the pressure control apparatus 80 increases the amount of refrigerant mass in the evaporator 60 while controlling back-feeding of liquid refrigerant to the compressor 65. The constant flow of the heated refrigerant during the defrost mode increases the temperature of the evaporator 60 and melts frost on the exterior of the evaporator 60.
The controller 120 utilizes a control process embodied by instructions in a processor to determine whether to initiate a demand defrost cycle and to control operation of the refrigeration system 45 in the cooling or refrigeration mode and in the defrost mode, and to determine additional factors and criteria as described in detail below. In one example, and with reference to
In general, and after determining the initial pressure differential Pinitial, which may be an average pressure differential over a period of time (e.g., 5 minutes), the controller 120 continuously or periodically monitors or determines the pressure differential P between the outlet tap 108 and the ambient tap 112 via the sensor 106. The controller 120 averages the detected pressure differential P along with previous pressure differential values (referred to as “historical pressure differentials” or Phistory) to identify an average pressure differential Pavg. For example, the controller 120 may average the pressure differential P and the immediately-previous nine (9) historical pressure differentials immediately preceding the detected pressure differential P (referred to herein as a “running average”).
With continued reference to
If the fan(s) 96 are determined to be On (“Yes” at step 310), the controller 120 determines whether a door 42 is open (step 325) when the merchandiser 10 includes doors 42 (step 325), or the controller 120 determines the pressure differential P (step 330). In merchandisers 10 with doors 42, when the controller 120 determines that a door 42 is open (“Yes” at step 325), the controller 120 determines whether the door 42 has been closed at step 335. If the door 42 has not been closed (“No” at step 335), the control process initiates a door alarm at step 340 when the alarm time for a door open condition has been met or exceeded (expired). The process then sets the length of time that the pressure differential P is below the pressure trigger value Tcount to zero and increments the time since last defrost cycle Tdef, and the process restarts at step 310.
If the door has been open less than the preset alarm time, the controller 120 continues to track or determine (at either or both of steps 335, 340) the amount of time the door has been open and the time since the previous defrost cycle. The controller 120 repeats steps 335, 340 until either the time the door has been open is greater than the preset alarm time or the door has been detected as closed. If the door is determined to be closed (“Yes” at step 335), the controller 120 determines the pressure differential P at step 330). It will be appreciated that steps 325-340 are omitted when the merchandiser 10 does not include doors.
Next, the control process determines whether the pressure differential P is less than the pressure trigger value Pset at step 345. If not (“No” at step 345), the control process sets the time of pressure drop Tfan to zero at step 350 and determines whether the pressure differential P is greater than the historical pressure differentials Phistory at step 355. If Yes at step 355, the process moves to step 320 and sets the length of time that the pressure differential P is below the pressure trigger value Tcount to zero and increments the time since last defrost cycle Tdef. The process restarts at step 310.
When the pressure differential P is not greater than the historical pressure differentials Phistory (“No” at step 355), the process determines whether the pressure differential P and historical pressure differentials Phistory are greater than zero, respectively. If Yes, the process determines the average pressure differential Pavg at step 365. The process then moves to step 320 and sets the length of time that the pressure differential P is below the pressure trigger value Tcount to zero and increments the time since last defrost cycle Tdef. Thereafter process restarts at step 310.
When the controller 120 determines that the pressure differential P is less than the pressure trigger value Pset at step 345, the controller 120 determines whether the pressure differential is less than the average pressure differential Pavg multiplied by a value representative of the threshold “R” at which the average pressure differential is indicative of abnormal operation for the refrigeration system 45 (e.g., representative of as sudden loss of airflow indicating a fan failure). For example, the threshold R may be a value between approximately 0% and 60% (e.g., 25%, 40%, 50%, etc.). The threshold When the controller 120 determines that the pressure differential is lower than the average pressure differential Pavg and the threshold R (“Yes” at step 370), the controller determines at step 375 whether time of the pressure drop Tfan is greater than a threshold alarm timeframe TalarmF. The alarm timeframe TalarmF may be any increment of time (e.g., 5 minutes, 3 minutes, 7 minutes, etc.) and is the threshold at which an alarm is triggered when the alarm timeframe TalarmF has been met or exceeded (step 380). The controller 120 initiates a timed defrost if the alarm timeframe TalarmF has been met or exceeded and personnel may be notified to shutdown the merchandiser 10. Thereafter process may restart at step 310.
If the pressure differential P is equal to or greater than the average pressure differential Pavg multiplied by the threshold R (“No” at step 385), the controller 120 sets the pressure drop Tfan to zero at step 350 and determines at step 390 whether the time Tcount is greater than the minimum time Tmin (the time determining whether to initiate demand defrost, e.g., 30 minutes). If not (“No” at step 390), the process moves to step 395 and increments the time Tcount and the time from previous defrost Tdef. The process then returns to step 310.
If the controller 120 determines that the time Tcount is greater than the minimum time Tmin (“Yes” at step 390), the process determines whether the time since last defrost cycle Tdef is greater than the minimum defrost wait time interval Tint at step 400. When the time since last defrost cycle Tdef is less than or equal to the minimum defrost wait time interval Tint (“No” at step 400), the control process moves to step 395 and increments the time Tcount and the time from previous defrost Tdef. The process then returns to step 310. When the time since last defrost cycle Tdef is greater than the minimum defrost wait time interval Tint (“Yes” at step 400), the control process determines at step 405 whether the current time (e.g., time of day) is within the refrigeration window. If so (“Yes” at step 405), the control process moves to step 395 and increments the time Tcount and the time from previous defrost Tdef. The process then returns to step 310. If the current time is not within the refrigeration window (“No” at step 405), the controller 120 initiates the demand defrost system and resets each of the pressure trigger value Tcount, the time since last defrost cycle Tdef, and the count for the average pressure differential (the running average) to zero and the process restarts after defrost is complete (e.g., the evaporator 60 is partially or fully defrosted based on input parameters input in the system). The defrost cycle may terminate based on a newly determined pressure differential P (e.g., via one or more processes in the control process described relative to
Because frost accumulation on the evaporator 60 is incremental and not exponential, sudden changes in the detected pressure differential may be interpreted as a potential failure associated with the merchandiser 10 (e.g., a door remaining open, a fan failure, etc.). Also, when a door 42 is closed, especially forcefully, the sensed pressure differential may significantly increase (e.g., 50-60% higher than a normal or expected pressure differential from the sensor 106). Likewise, when a door 42 is opened, the suction created may significantly lower the pressure differential that is sensed by the sensor 106. In these situations, the pressure differential reading is ignored by the system.
The airflow induced by the fan 96 reduces as the static pressure drops across the evaporator 60 due to frost accumulation during refrigeration cycles. Demand defrost embodied in the invention described and claimed herein can be applied either as a standalone device to signal a storewide controller or implemented within a case-level controller for merchandisers or freezers with doors to reduce or eliminate frost accumulation. The controller monitors the air pressure outside the case relative to the air downstream of the evaporator coil. Additional inputs may optionally include door position, fan operation, and user specified time windows that are unacceptable for defrost cycles. The invention embodied herein and in the claims may be applied to drawn airflow or forced airflow configurations using one or more sensors to determine the pressure differential between ambient air and air downstream of the evaporator. In some embodiments, could potentially configure itself on various units without manual adjustment.
The system embodying the invention described and claimed herein is non-invasive to the evaporator and the airflow inside the merchandiser. The system does not require sensors in the heat transfer area of the evaporator and fins of the evaporator do not need to be adjusted or trimmed which would have a negative impact on coil performance. This method for demand defrost also does not require large data collection, therefore lower cost controllers can be utilized and less sensors are required in the case to monitor frost accumulation. This control model could also be adjusted to monitor open door conditions and evaporator fan failures. An advantage associated with the demand defrost system described herein is that the system determines the defrost trigger value based on the pressure differential reading (Pinitial) on startup of the merchandiser read upon starting the case. This allows the demand defrost system to be applied to multiple cases and configurations without testing each application of the system to find the proper pressure trigger value.
Although the invention has been described in detail with reference to certain preferred embodiments, variations and modifications exist within the scope and spirit of one or more independent aspects of the invention as described. It will be appreciated that each feature of the merchandiser 10 and each feature of the control system may form the basis of one or more claims on its own or in any combination with any other feature or features. The order in which the control system is described (e.g., in
Various features and advantages of the invention are set forth in the following claims.
This application claims priority to U.S. Provisional Patent Application No. 63/376,656, filed on Sep. 22, 2022, and entitled “Refrigeration System With Fluid Defrost”, the content of which is hereby incorporated by reference in its entirety.
Number | Date | Country | |
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63376656 | Sep 2022 | US |