The invention relates to refrigerator cases. More particularly, the invention relates to coil configurations and routing in open-front cases.
Refrigerated cases (generically including both freezers and refrigerator-only units) are used in a variety of commercial situations. One key use is for retail display and vending. Many such cases include a closed rear wall and either an open front or a glass door front. U.S. Pat. No. 6,460,372, the disclosure of which is incorporated by reference herein as if set forth at length, discloses an exemplary open-front refrigerated case configuration.
Providing a forced air flow through the compartment of such cases is important for a number of reasons. Maintaining the desired food temperature in view of exposure to room air is an important factor. Moisture transport is another (e.g., to control undesirable condensation). One common forced flow scheme involves a cold air curtain downwardly discharged from a front top area of the compartment. A return flow is drawn through an intake at the bottom front of the compartment.
The return flow may be drawn across a cooling heat exchanger (e.g., evaporator coils), typically in a base of the case. The cooled air passes upward through a rear duct at the back of the compartment. The cooled air then passes forward through a top duct. at the front of the top duct, the air is turned downward by turning vanes to form the air curtain. The rear and top ducts may respectively be defined between rear and top insulated panels and non-insulated rear and top duct panels along the rear and top of the compartment.
One aspect of the invention involves a refrigerated case having a housing containing an interior volume for storing items. An air flow path extends from an air inlet to an air outlet. A fan is positioned to drive an air flow along the air flow path. The air outlet is positioned to discharge cold air to cool the interior volume. A refrigerant-to-air heat exchanger is positioned along the air flow path. A refrigerant flow path passes through the heat exchanger. An expansion device is located along the refrigerant flow path.
Along the air flow path, the heat exchanger has evaporator and reheat sections. A preconditioning section (if any) may be upstream of the evaporator section and the evaporator section is upstream of the reheat section.
Along the refrigerant flow path, the reheat section is downstream of the preconditioning section (if any) and upstream of the evaporator section and the expansion device is between the reheat and evaporator sections.
The details of one or more embodiments of the invention are set forth in the accompanying drawings and the description below. Other features, objects, and advantages of the invention will be apparent from the description and drawings, and from the claims.
Like reference numbers and designations in the various drawings indicate like elements.
The exemplary base 30 may include front and back transverse rails or 50 and 52 for supporting the remainder of the base and, therethrough, the remainder of the case atop a ground/floor surface. The exemplary base 30 contains at least a portion of the refrigeration equipment (e.g., a heat exchanger 60 functioning in part as an evaporator and an expansion device 62, shown schematically in
The air flow passes through the heat exchanger 60 as is discussed in further detail below. After exiting the heat exchanger 60, the air flow passes upward through a rear section of the air flow path 510 in a duct 74. The air flow then proceeds forward through a top duct 76 and exits the top duct through an outlet 78 (e.g., a group of vanes or a honeycomb directing the outlet/discharge flow 512 downward along the front of the case). One or more branch air flows 514 may branch off (e.g., through apertures in the wall 79 of the duct 74).
The exemplary heat exchanger 60 is a refrigerant-to-air heat exchanger through which the refrigerant flow path 520 also passes. Along the refrigerant flow path 520, the first section 110 is also an upstream section, receiving the refrigerant flow 518 through the inlet 96. The first section 110 is, however, coupled to deliver the refrigerant flow to the third section 114 downstream thereof, bypassing the second section 112. Refrigerant exiting the third section 114 is expanded in the expansion device 62 (e.g., a thermal expansion valve (TXV)) then delivered to the second section 112 via a distribution manifold 118. Refrigerant exits the second section 112 through the outlet 82 to return to the compressor.
Accordingly, the heat exchanger second section 112 acts as an evaporator. The third section 114 serves as a reheat section operating in conjunction with the evaporator (e.g., s may play roles in moisture control.
In the exemplary heat exchanger, there are three tubes in the upstreammost (first/leading) group, in the three central positions. The inlet 96 is formed at one end (e.g., the right end) of one of these tubes (e.g., the lowest). The refrigerant flow in the first section 110 thus proceeds through this tube, then through one of the U-connectors 128 to the second tube immediately above and then through another of the U-connectors to the third tube yet above the second tube. The refrigerant flow then traverses through a long connector conduit/line (“jumper”) 140 to the last group of tubes (the third section 114). In the exemplary heat exchanger, the connector 140 connects to one end (e.g., the left end) of one of the tubes (e.g., a tube in the uppermost of the five available positions) and then through one of the connectors 128 to the next tube therebelow and then through another of the connectors 128 to the tube therebelow. In the exemplary heat exchanger, the lower two tube positions in the downstreammost group are empty. This particular configuration was selected because the air flow exiting the heat exchanger is directed upward to pass through the rear duct 74. Accordingly, the air flow has the greatest exposure to tubes in the high positions of the downstreammost group. The refrigerant exiting the last tube in this final group then enters a conduit 150 (
Although a basic dehumidification function may be achieved by use of pre-expansion refrigerant in the third section 114, alone, use of the first section 110 may have one or more of several advantages.
A given refrigerated case or model thereof may experience a wide range of ambient temperature conditions. A given case will experience seasonal changes, shorter term weather variations, daily temperature fluctuations and factors relating to siting within a particular store. More broadly, a given model may have to accommodate a wide variety of geographic locations, thereby exacerbating the required range of accommodation.
For an air cooled condensing unit, the condensing temperature and drop leg liquid refrigerant temperature is affected by the outdoor air temperature and system design. It is common that liquid refrigerant temperature enter the housing at 20-90° F.
For a medium temperature merchandiser operation, return air feeding into the heat exchanger is typically 38-46° F. depending on store ambient temperature, merchandise loading condition, and display configuration (e.g., peg bar, shelf etc.). After exchanging heat with refrigerant in the evaporator, air exiting a typical evaporator is typically 29-34° F. (depending on average coil temperature and system dynamic). The air temperature typically increases by 1-2° F. before discharge from the outlet 78.
For dairy, deli, beverage, and produce application, a discharge air temperature of 33-36° F. is common to keep products at the desired temperature.
In an exemplary summer condition without the first section 110, relatively warm (e.g., ˜90° F.) liquid refrigerant enters the reheat section of the coil directly. Thus there is a large temperature difference (˜60° F.) between the liquid refrigerant and the air exiting the evaporator (low 30's° F.). With high coil efficiency, after exchanging heat with the liquid refrigerant, the dry bulb temperature of air exiting the reheat section can increase by as much as 3° F. above that of the air exiting the evaporator. The relative humidity will drop from 99% to 78%. However, the temperature of air exiting the outlet can rise above acceptable range in some operating condition. And there might be an issue with product temperature.
With the first section 110, the warm (e.g., ˜90° F.) liquid refrigerant enters the first section and exchanges heat with return air (e.g., at ˜43° F.). The temperature of the liquid refrigerant will drop substantially (e.g., to ˜46° F.) after passing sequentially through the three tubes of the first section 110. This cooled liquid refrigerant is then fed into the third (reheat) section 114 of the heat exchanger by the jumper conduit 140. The refrigerant then exchanges heat with the air exiting the evaporator 112 (at low 30's° F.), raising the air dry bulb by 1-2° F. (depending on location). This reduces the air relative humidity from 99% exiting the evaporator 112 to a range of ˜90-95% exiting the reheat section 114. This dehumidification is sufficient (e.g., to absorb any condensation due to defrost & temperature cycles, infiltration due to merchandise overloading or other reason) and also is still sufficiently cold.
In the exemplary third section 114, only the uppermost three tube locations are used and the flow starts in the upper most tube and proceeds downward. These two factors impose a reheat gradient across the airflow, with the most reheated air exiting the heat exchanger near the top. Due to flow stratification, it is this warmest air (and lowest relative humidity) that will pass into the case interior near the bottom of the rear duct. Because condensation is often worst near the bottom of prior art cases, this stratification directs the driest air to where it is most required.
In an exemplary winter condition without the first section 110, liquid refrigerant enters the reheat section of the heat exchanger at a very low temperature (e.g., in the low 20's° F., or as low as 0° F.). This temperature may be even lower than the temperature of the air exiting the evaporator (e.g., in the low 30's° F.) to encounter it. Instead of raising the dry bulb temperature of the air, the refrigerant will further cool the air and produce an exit air relative humidity slightly higher than that of the air exiting the evaporator.
With the first section 110, the very low temperature liquid refrigerant enters the first section where it encounters return air at an exemplary temperature of ˜38° F. (low store ambient temperature resulting in a lower return air temperature than in the summer). In the first section, the liquid refrigerant temperature is then raised to ˜37.4° F. and fed into the reheat section 114 of the heat exchanger by the jumper conduit 140. In the third section 114, the liquid refrigerant then exchanges heat with air exiting the evaporator section 112 (e.g., ˜30° F.). The air dry bulb would be raised by ˜0.6 F, lowering the air relative humidity from ˜97.4% exiting the evaporator 112 (in winter, the relative humidity of the air exiting evaporator tends to be lower than in summer) to ˜94.8% exiting the reheat section. In a variation, if the liquid refrigerant entered the heat exchanger at 25° F. air exiting the reheat section would have 94.2% relative humidity with the first section.
The general effect of the first section is to moderate the liquid refrigerant temperature of the third section (e.g. to a ˜37-50° F. range instead of a ˜0-90° F. range). All other things being equal, the addition of the first and third sections produces a discharge air temperature slightly higher than without. Air distribution optimization in the display case may compensate for the slightly higher air temperature so as to maintain the temperature of merchandise in an acceptable range. Alternative optimizations may involve coil resizing.
One or more embodiments of the present invention have been described. Nevertheless, it will be understood that various modifications may be made without departing from the spirit and scope of the invention. For example, the foregoing teachings may be applied in the reengineering of an existing case configuration. In such a reengineering, details of the existing configuration will influence or dictate details of any particular implementation. This may include open top cases and closed cases. Accordingly, other embodiments are within the scope of the following claims.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/US2005/043033 | 11/28/2005 | WO | 00 | 4/7/2008 |
Publishing Document | Publishing Date | Country | Kind |
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WO2007/061420 | 5/31/2007 | WO | A |
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Number | Date | Country | |
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20080271473 A1 | Nov 2008 | US |