Patent Grant
6955061
The present invention relates generally to refrigerated merchandiser systems and, more particularly, to a refrigerated, medium temperature, merchandiser system for displaying food and/or beverage products.
In conventional practice, supermarkets and convenient stores are equipped with display cases, which may be open or provided with doors, for presenting fresh food or beverages to customers, while maintaining the fresh food and beverages in a refrigerated environment. Typically, cold, moisture-bearing air is provided to the product display zone of each display case by passing air over the heat exchange surface of an evaporator coil disposed within the display case in a region separate from the product display zone so that the evaporator is out of customer view. A suitable refrigerant, such as for example R-404A refrigerant is passed through the heat exchange tubes of the evaporator coil. As the refrigerant evaporates within the evaporator coil, heat is absorbed from the air passing over the evaporator so as to lower the temperature of the air.
A refrigeration system is installed in the supermarket and convenient store to provide refrigerant at the proper condition to the evaporator coils of the display cases within the facility. All refrigeration systems include at least the following components: a compressor, a condenser, at least one evaporator associated with a display case, a thermostatic expansion valve, and appropriate refrigerant lines connecting these devices in a closed circulation circuit. The thermostatic expansion valve is disposed in the refrigerant line upstream with respect to refrigerant flow of the inlet to the evaporator for expanding liquid refrigerant. The expansion valve functions to meter and expand the liquid refrigerant to a desired lower pressure, selected for the particular refrigerant, prior to entering the evaporator. As a result of this expansion, the temperature of the liquid refrigerant also drops significantly. The low pressure, low temperature liquid evaporates as it absorbs heat in passing through the evaporator tubes from the air passing over the surface of the evaporator. Typically, supermarket and grocery store refrigeration systems include multiple evaporators disposed in multiple display cases, an assembly of a plurality of compressors, termed a compressor rack, and one or more condensers.
Additionally, in certain refrigeration systems, an evaporator pressure regulator (EPR) valve is disposed in the refrigerant line at the outlet of the evaporator. The EPR valve functions to maintain the pressure within the evaporator above a predetermined pressure set point for the particular refrigerant being used. In refrigeration systems used to chill water, it is known to set the EPR valve so as to maintain the refrigerant within the evaporator above the freezing point of water. For example, in a water chilling refrigeration system using R-12 as refrigerant, the EPR valve may be set at a pressure set point of 32 psig (pounds per square inch, gage) which equates to a refrigerant temperature of 34 degrees F.
In conventional practice, evaporators in refrigerated food display systems generally operate with refrigerant temperatures below the frost point of water. Thus, frost will form on the evaporators during operation as moisture in the cooling air passing over the evaporator surface comes in contact with the evaporator surface. In medium temperature refrigeration display cases, such as those commonly used for displaying produce, milk and other dairy products, or beverages in general, the refrigerated product must be maintained at a temperature typically in the range of 32 to 41 degrees F. depending upon the particular refrigerated product. In medium temperature produce display cases for example, conventional practice in the field of commercial refrigeration has been to pass the circulating cooling air over the tubes of an evaporator in which refrigerant passing through the tubes boils at about 21 degrees F. to maintain the cooling air temperature at about 31 or 32 degrees F. In medium temperature dairy product display cases for example, conventional practice in the commercial refrigeration field has been to pass the circulating cooling air over the tubes of an evaporator in which refrigerant passing through the tubes boils at about 21 degrees F. to maintain the cooling air temperature at about 28 or 29 degrees F. At these refrigerant temperatures, the outside surface of the tube wall will be at a temperature below the frost point. As frost builds up on the evaporator surface, the performance of the evaporator deteriorates and the free flow of air through the evaporator becomes restricted and in extreme cases halted.
Fin and tube heat exchanger coils of the type having simple flat fins mounted on refrigerant tubes that are commonly used as evaporators in the commercial refrigeration industry characteristically have a low fin density, typically having from 2 to 4 fins per inch. Customarily, in medium temperature display cases, an evaporator and a plurality of axial flow fans are provided in a forced air arrangement for supplying refrigerated air to the product area of the display case. Most commonly, the fans are disposed upstream with respect to air flow, that is in a forced draft mode, of the evaporator in a compartment beneath the product display area, with there being one fan per four-foot length of merchandiser. That is, in a four-foot long merchandiser, there would typically be one fan, in an eight-foot long merchandiser there would be two fans, and in a twelve-foot long merchandiser there would be three fans. In operation, the fan forces the air through the evaporators, passing over the tubes of the fin and tube exchanger coil, and circulates the refrigerated air through a flow duct on the backside of the merchandiser housing and thence through a flow duct at the top of the merchandiser housing to exit into the product display area. In open-front display case configurations, the refrigerated air exiting the upper flow duct passes generally downwardly across the front of the product display area to form an air curtain separating the product display area from the ambient environment of the store, thereby reducing infiltration of ambient air into the product display area.
As previously noted, it has been conventional practice in the commercial refrigeration industry to use only heat exchangers of low fin density in evaporators for medium temperature applications. This practice arises in anticipation of the buildup of frost of the surface of the evaporator heat exchanger and the desire to extend the period between required defrosting operations. As frost builds up, the effective flow space for air to pass between neighboring fins becomes progressively less and less until, in the extreme, the space is bridged with frost. As a consequence of frost buildup, heat exchanger performance decreases and the flow of adequately refrigerated air to the product display area decreases, thus necessitating activation of the defrost cycle. Additionally, since the pressure drop through a low fin density evaporator coil is relatively low, such a low pressure drop in combination with a relatively wide spacing between fans as mentioned hereinbefore, results in a significant variance in air velocity through the evaporator coil which in turn results in an undesirable variance, over the length of the evaporator coil, in the temperature of the air leaving the coil. Temperature variances of as high as 6° F. over a span as small as eight inches, are not atypical. Such stratification in refrigeration air temperature can potentially have a large effect on product temperature resulting in undesirable variation in product temperature within the product display area.
When frost forms on the evaporator coil, it tends to accumulate in areas where there is low airflow velocity to begin with. As a result, airflow is further maldistributed and temperature distribution becomes more distorted. Air flow distribution through the evaporator is also distorted as a result of the inherent air flow velocity profile produced by a plurality of conventionally spaced axial flow fans. As each fan produces a bell-curve like velocity flow, the air flow velocity profile is characteristically a wave pattern, with air flow velocity peaking near the centerline of each fan and dipping to a minimum between neighboring fans.
U.S. Pat. No. 5,743,098, Behr, discloses a refrigerated food merchandiser having a modular air cooling and circulating means comprising a plurality of modular evaporator coil sections of a predetermined length, each evaporator coil section having a separate air moving means associated therewith. The evaporator coils are arranged in horizontal, spaced, end-to-end disposition in a compartment beneath the product display area of the merchandiser. A separate pair of axial flow fans is associated with each evaporator section for circulating air from an associated zone of the product display zone through the evaporator coil for cooling, and thence back to the associated zone of the product display area.
It is an object of this invention to provide an improved medium temperature merchandiser having an improved air flow distribution entering the evaporator.
It is a further object of this invention to provide a refrigerated merchandiser having an evaporator characterized by a relatively more uniform exit air temperature across the length of the evaporator.
A refrigerated merchandiser is provided having an insulated cabinet defining a product display area and a compartment separate from the product display area wherein an evaporator and a plurality of laterally spaced, air circulating fan are disposed. The evaporator is disposed downstream of the plurality of laterally spaced fans. That is, the fans are in a forced draft mode relative to the evaporator, whereby the fans force circulating air through the evaporator. In accordance with the present invention, a flow baffle is disposed intermediate the evaporator and the fans. The flow baffle functions to redistribute the airflow from the flow pattern conventionally associated with such a plurality of laterally spaced fans to a relatively more uniform flow pattern. The flow baffle may comprise a single multi-apertured member, such as a perforated planar member, a screen mesh member, a slotted planar member, a planar member having a honeycomb passageway structure or an equivalent member.
Alternatively, the flow baffle may comprise a plurality of such multi-apertured members stacked in axially spaced relationship along the flow path between the fans and the evaporator.
For a further understanding of the present invention, reference should be made to the following detailed description of a preferred embodiment of the invention taken in conjunction with the accompanying drawings wherein:
The refrigeration system is illustrated in
Referring now to
The refrigerated merchandiser 100, commonly referred to as a display case, includes an upright, open-front, insulated cabinet 110 defining a product display area 125. The evaporator 40, which is a fin and tube heat exchanger coil, is disposed within the refrigerated merchandiser 100 in a compartment 120 separate from and, in the depicted embodiment, beneath the product display area 125. The compartment 120 may, however, be disposed above or behind the product display area as desired. As in convention practice, air is circulated by air circulation means 70, disposed in the compartment 120, through the air flow passages 112, 114 and 116 formed in the walls of the cabinet 110 into the product display area 125 to maintain products stored on the shelves 130 in the product display area 125 at a desired temperature. A portion of the refrigerated air passes out the airflow passage 116 generally downwardly across the front of the display area 125 thereby forming an air curtain between the refrigerated product display area 125 and the ambient temperature in the region of the store near the display case 100.
The expansion device 50, which is generally located within the display case 100 close to the evaporator 40, but may be mounted at any location in the refrigerant line 14, serves to meter the correct amount of liquid refrigerant flow into the evaporator 40. As in conventional practice, the evaporator 40 functions most efficiently when as full of liquid refrigerant as possible without passing liquid refrigerant out of the evaporator into suction line 18. Although any particular form of conventional expansion device may be used, the expansion device 50 most advantageously comprises a thermostatic expansion valve (TXV) 52 having a thermal sensing element, such as a sensing bulb 54 mounted in thermal contact with suction line 18 downstream of the outlet 44 of the evaporator 40. The sensing bulb 54 connects back to the thermostatic expansion valve 52 through a conventional capillary line 56.
The evaporator pressure control device 60, which may comprise a stepper motor controlled suction pressure regulator or any conventional evaporator pressure regulator valve (collectively EPRV), operates to maintain the pressure in the evaporator at a preselected desired operating pressure by modulating the flow of refrigerant leaving the evaporator through the suction line 18. By maintaining the operating pressure in the evaporator at that desired pressure, the temperature of the refrigerant expanding from a liquid to a vapor within the evaporator 40 will be maintained at a specific temperature associated with the particular refrigerant passing through the evaporator.
Referring now to
The evaporator 40 preferably comprises a fin and tube heat exchanger coil 42 having a relatively high fin density, that is a fin density at least five fins 44 per inch of tube 46, as compared to the relatively low fin density fin and tube heat exchanger coils commonly used in conventional medium temperature display cases. Due to the relatively high fin density, the pressure drop experienced by circulating air passing through the evaporator coil is significantly higher, typically on the order of 2 to 8 times greater, than the pressure drop experienced under similar flow conditions by circulating air passing through a conventional low fin density fin and tube evaporator coil. This increased flow resistance through the high fin density evaporator coil results in a more uniform air flow distribution through the evaporator. Most advantageously, the relatively high density fin and tube heat exchanger coil 42 of the high efficiency evaporator 40 has a fin density in the range of six to fifteen fins per inch. The relatively high fin density heat exchanger coil 42 is capable of operating at a significantly lower differential of refrigerant temperature to evaporator outlet air temperature than the differential at which conventional low fin density evaporators operate.
The high fin density heat exchanger coil of the high efficiency evaporator 40 is also more compact in volume than conventional commercial refrigeration evaporators of comparable heat exchange capacity. For example, the evaporator for the model L6D8 medium-temperature display case manufactured by Tyler Refrigeration Corporation of Niles, Mich., which is designed to operate with a refrigerant temperature of 20 degrees F. It has a fin and tube heat exchanger of conventional design having 10 rows of ⅝ inch diameter tubes having 2.1 fins per inch, providing about 495 square feet of heat transfer surface in a volume of about 8.7 cubic feet. With the high fin density, high efficiency evaporator 40 installed in the model L6D8 case, the display case was successfully operated in a relatively frost-free mode in accordance with the present invention. The high efficiency evaporator operated with a refrigerant temperature of 29 degrees F. In comparison to the aforedescribed conventional heat exchanger, the high fin density heat exchanger of the high efficiency evaporator has 8 rows of ⅜ inch diameter tubes having 10 fins per inch, providing about 1000 square feet of heat transfer area in a volume of about 4.0 cubic feet. Thus, in this application, the high efficiency evaporator 40 provides nominally twice the heat transfer surface area while occupying only half the volume of the conventional evaporator.
Referring now to
As each particular refrigerant has its own characteristic temperature-pressure curve, it is theoretically possible to provide for frost-free operation of the evaporator 40 by setting EPRV 60 at a predetermined minimum pressure set point for the particular refrigerant in use. In this manner, the refrigerant temperature within the evaporator 40 may be effectively maintained at a point at which all external surfaces of the evaporator 40 in contact with the moist air within the refrigerated space are above the frost formation temperature. However, due to structural obstructions or airflow maldistribution over the evaporator coil, some locations on the coil may fall into a frost formation condition leading to the onset of frost formation.
Advantageously, a controller 90 may be provided to regulate the set point pressure at which the EPRV 60 operates. The controller 90 receives an input signal from at least one sensor operatively associated with the evaporator 40 to sense an operating parameter of the evaporator 40 indicative of the temperature at which the refrigerant is boiling within the evaporator 40. The sensor may comprise a pressure transducer 92 mounted on suction line 18 near the outlet 43 of the evaporator 40 and operative to sense the evaporator outlet pressure. The signal 91 from the pressure transducer 92 is indicative of the operating pressure of the refrigerant within the evaporator 40 and therefore, for the given refrigerant being used, is indicative of the temperature at which the refrigerant is boiling within the evaporator 40. Alternatively, the sensor may comprise a temperature sensor 94 mounted on the coil of the evaporator 40 and operative to sense the operating temperature of the outside surface of the evaporator coil. The signal 93 from the temperature sensor 94 is indicative of the operating temperature of the outside surface of the evaporator coil and therefore is also indicative of the temperature at which the refrigerant is boiling within the evaporator 40. Advantageously, both a pressure transducer 92 and a temperature sensor 94 may be installed with input signals being received by the controller 90 from both sensors thereby providing safeguard capability in the event that one of the sensors fails in operation.
The controller 90 determines the actual refrigerant boiling temperature at which the evaporator is operating from the input signal or signals received from sensor 92 and/or sensor 94. After comparing the determined actual refrigerant boiling temperature to the desired operating range for refrigerant boiling temperature, the controller 90 adjusts, as necessary, the set point pressure of the EPRV 60 to maintain the refrigerant boiling temperature at which the evaporator 40 is operating within a desired temperature range.
The refrigerated merchandiser system 10 may be operated in accordance with a particularly advantageous method of operation described in detail in commonly assigned, co-pending U.S. Pat. application Ser. No. 09/652,353, filed Aug. 31, 2000. In accordance with this method of operation, the controller 90 functions to selectively regulate the set point pressure of the EPRV 60 at a first set point pressure for a first time period and at a second set point pressure for a second time period and to continuously cycle the EPRV 60 between the two set point pressure. The first set point pressure is selected to lie within the range of pressures for the refrigerant in use equivalent at saturation to a refrigerant temperature in the range of 24 degrees F. to 32 degrees F., inclusive. The second set point pressure is selected to lie within the range of pressures for the refrigerant in use equivalent at saturation to a refrigerant temperature in the range of 31 degrees F. to 38 degrees F., inclusive. Therefore, the refrigerant boiling temperature within the evaporator 40 of the medium temperature display case 100 is always maintained at a refrigerating level, cycling between a first temperature within the range of 24 degrees F. to 32 degrees F. for a first time period and a second slightly higher temperature within the range of 31 degrees F. to 38 degrees F. for a second period. In this cyclic mode of operation, the evaporator 40 operates continuously in a refrigeration mode, while any undesirable localized frost formation that might occur during the first period of operation cycle at the cooler refrigerant boiling temperatures is periodically eliminated during second period of the operating cycle at the warmer refrigerant boiling temperatures. Typically, it is advantageous to maintain the refrigerant boiling temperature within the evaporator during the second period of an operation cycle at about 2 to about 12 degrees F. above the refrigerant boiling temperature maintained during the first period of the operation cycle.
Although, the respective durations of the first period and the second period of the operation cycle will varying from display case to display case, in general, the first time period will substantially exceed the second time period in duration. For example, a typical first time period for operation at the relatively cooler refrigerant boiling temperature will extend for about two hours up to several days, while a typical second time period for operation at the relatively warmer refrigerant boiling temperature will extend for about fifteen to forty minutes. However, the operator of the refrigeration system may selectively and independently program the controller 90 for any desired duration for the first time period and any desired duration for second time period without departing from the spirit and scope of the present invention.
In transitioning from operation at the relatively cooler refrigerant boiling temperature to continued refrigeration operation at the relatively warmer refrigerant boiling temperature, it may be advantageous to briefly maintain steady-state operation at an intermediate temperature of about 31 to about 32 degrees F. The time period for operation at this intermediate temperature would generally extend for less than about ten minutes, and typically from about four to about eight minutes. Such an intermediate steady-state stage may be desirable, for example on single compressor refrigeration systems, as a means of avoiding excessive compressor cycling. In sequencing back from operation at the relatively warmer refrigerant boiling temperature to operation at the relatively cooler refrigerant boiling temperature, no intermediate steady-state stage is provided.
The flow baffle 150 of the present invention is operative to improve the uniformness of the air flow entering the evaporator independent of the number of fans 70 upstream of the evaporator 40. In a conventional twelve-foot long refrigerated merchandiser, three fans, spaced four feet apart between adjacent fans, are provided in the conventional embodiment. Increasing the number of fans 70, thereby decreasing the spacing between adjacent fans, further improves air flow distribution uniformity along the length of the evaporator. Even if the number of fans were decreased, use of the flow baffle 150 would intermediate the fans and the evaporator would result in a more uniform air flow velocity profile entering the evaporator than would exist without the flow baffle 150 being present.
Although a preferred embodiment of the present invention has been described and illustrated, other changes will occur to those skilled in the art. For example, the present invention may be practiced on refrigerated merchandisers whether or not using the disclosed electronic controller 90, its associated sensors or the disclosed method of operation. It is therefore intended that the scope of the present invention is to be limited only by the scope of the appended claims.
This application is a continuation-in-part of commonly assigned application Ser. No. 09/573,308, filed May 18, 2000 now U.S. Pat. No. 6,311,512, for Refrigerated Merchandiser System.
| Number | Name | Date | Kind |
|---|---|---|---|
| 5408921 | Persson et al. | Apr 1995 | A |
| Number | Date | Country | |
|---|---|---|---|
| 20010042383 A1 | Nov 2001 | US |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 09573308 | May 2000 | US |
| Child | 09747920 | US |
