The present invention relates generally to a display case including a heat exchanger that reduces the relative humidity of air exiting the heat exchanger.
Refrigerated food and beverage display cases are commonly used in grocery stores or supermarkets to cool refrigerated products and present the products to customers in an appealing manner. A heat exchanger cools the air in the display case, and a fan system generates an air curtain that cools the products in the display case. If the relative humidity of the air exiting the heat exchanger is too high, moisture can condense on the packaging of the products, possibly affecting the structural integrity of the packaging.
Hence, there is need in the art for a display case including a heat exchanger that reduces the relative humidity of air exiting the heat exchanger and that overcomes the drawbacks and shortcomings of the prior art.
A display case cools products and presents the products to customers in an appealing manner. A heat exchanger cools air in the display case to a desired temperature, and a fan system circulates the cooled air through the display case to cool the products to a desired temperature. If warm ambient air enters an interior display volume of the display case, localized condensation on the products can occur.
The heat exchanger includes a circuit defined by a heat exchanger section including a plurality of tubes that define a flow path, a reheat section including a reheat tube, and a connecting tube fluidly connecting the flow path of the heat exchanger section with the reheat tube. Air flows over the plurality of tubes of the heat exchanger section and rejects heat to a refrigerant flowing through the plurality of tubes to heat the refrigerant. The heated refrigerant then flows through the reheat tube. As the air passes over the reheat tube, the air accepts heat from the heated refrigerant flowing through the reheat tube.
As the air flows over the reheat tube, the warmed refrigerant slightly warms the air, raising the dew point of the air and lowering the relative humidity of the air exiting the heat exchanger. The lower relative humidity air has more capacity to remove any moisture that might have been deposited inside the interior display volume, preventing localized condensation on the products.
These and other features of the present invention will be best understood from the following specification and drawings.
The various features and advantages of the invention will become apparent to those skilled in the art from the following detailed description of the currently preferred embodiment. The drawings that accompany the detailed description can be briefly described as follows:
A fan system 16 circulates cool air through the display case 10 to cool the products 12 to a desired temperature. The fan system 16 includes a fan 18 located at a bottom front of the display case 10. The fan 18 draws air through a return grille 20 and into a heat exchanger 22.
The air 64 drawn into the heat exchanger 22 by the fan 18 is approximately 41° F. The air 64 flows through the heat exchanger 22 (which is part of a chiller system also including a compressor, not shown) that cools the air 64 to a desired temperature, usually approximately 30 to 31° F. The air 64 exchanges heat with a refrigerant flowing through the heat exchanger 22 to cool the air 64 and therefore the product 12. The air 64 flows in a generally horizontal direction through the heat exchanger 22. In one example, the refrigerant is a secondary heat transfer fluid, such as a glycol/water solution. In one example, the secondary heat transfer fluid is a non-evaporative fluid.
After exiting the heat exchanger 22, the cooled air then flows upwardly in a generally vertical direction through a rear duct 24. The rear duct 24 is separated from the interior display volume 26 by a rear duct panel 28. Part of the air moving up the rear duct 24 also diffuses into the interior display volume 26 through holes 30 in the rear duct panel 28 and flows in a generally horizontal direction to help refrigerate the products 12 in the interior display volume 26.
The air then flows generally horizontally through an upper conduit 32 to an upper front of the display case 10. The air flows through a discharge grille 34 and is discharged downwardly and generally vertically towards a floor 36 to form an air curtain 38. The air curtain 38 cools the products 12 in the display case 10, separating the interior display volume 26 from ambient air 40 external to the display case 10. Typically, the ambient air 40 is approximately 70-75° F. The air then flows through the return grille 20 and into the fan system 16, completing the air circulation cycle.
As the air 64 flows though the heat exchanger 22, it exchanges heat with a refrigerant flowing through the heat exchanger 22. When a high efficiency heat exchanger 22 is employed, the air 64 exiting the heat exchanger 22 approaches the temperature of the refrigerant in the heat exchanger 22. This can especially occur in the winter, when the temperature of the ambient air 40 in the store is lower (for example, to save on heating costs of the store). This reduces the loading on the heat exchanger 22, causing the heat exchanger 22 to be oversized. The relative humidity of the air 64 exiting the heat exchanger 22 approaches 100%.
If any of the products 12 protrude into and disrupt the air curtain 38, the warm ambient air 40 can migrate into the interior display volume 26. The dew point of the outside air is usually significantly higher than the temperature inside the display case 10. If the ambient air 40 mixes with the cold air inside the display case 10, the ambient air 40 drops below its dew point. The air 64 that is just exiting the heat exchanger 22 inside the display case 10 is already close to saturation, and the air in the display case 10 has little capacity to absorb the moisture separated from the ambient air 40.
Localized condensation can form on the products 12 and the shelves 14 in the display case 10. If the products 12 have cardboard packaging, the packaging can absorb the moisture condensed on its surface and become soggy over time, causing the packaging to lose its structural integrity and break down when handled.
The temperature of the refrigerant entering the heat exchanger 22 is approximately 25-27° F., and the temperature of the refrigerant exiting the heat exchanger 22 is approximately 28 to 31° F. The air 64 flows around the plurality of tubes 46, and the refrigerant flows through the plurality of tubes 46. In one example, the plates 42 and 44 are made of steel, the plurality of tubes 46 are made of copper, and the fins 70 are made of aluminum.
The heat exchanger 22 includes at least one heat exchanger circuit having a heat exchanger section and at least one reheat circuit having a heat exchanger section and a reheat section.
As the air 64 flows through the heat exchanger 22, the air 64 rejects heat to the refrigerant flowing through the plurality of tubes 46 in the heat exchanger section of the heat exchanger 22. In
Returning to
In row A, refrigerant enters the heat exchanger 22 at 52 and flows in a first direction (into the page of
Although only the heat exchanger circuit defined by the tubes 46a, 46b, 46c and 46d of row A has been illustrated and described, the tubes 46 in each of the rows B, C, F, G and J can also define a heat exchanger circuit. In one example, the heat exchanger 22 includes six heat exchanger circuits. Refrigerant enters each of the six heat exchanger circuits defined by rows A, B, C, F, G and J at 52, makes four passes through the heat exchanger 22, and exits the heat exchanger 22 at 54.
In one example, the heat exchanger 22 includes two reheat circuits that include both a heat exchanger section and a reheat section. A first reheat circuit primarily uses the holes 48 in rows D and E, and a second reheat circuit primarily uses the holes in rows H and I.
In the first reheat circuit, the refrigerant generally flows back and forth between rows D and E. As the refrigerant flows through the heat exchanger section of the first reheat circuit, the refrigerant moves from the outlet side 60 of the heat exchanger 22 to the inlet side 62 of the heat exchanger 22 generally perpendicular to the air 64 flow.
The refrigerant enters the heat exchanger 22 at 52 and flows through a tube 46 received in the holes 48E3 of the plates 42 and 44. The refrigerant flows through a connecting tube 56a connected near the plate 44 and enters a tube 46 received in the holes 48D4 of the plates 42 and 44 and flows towards the plate 42. The refrigerant flows through a connecting tube 56b connected near the plate 42 and enters a tube 46 received in the holes 48E5 of the plates 42 and 44 and flows towards the plate 44. The refrigerant flows through a connecting tube 56c connected near the plate 44 and enters a tube 46 received in the holes 48D6 of the plates 42 and 44 and flows towards the plate 42. The refrigerant flows through a connecting tube 56d connected near the plate 42 and enters a tube 46 received in the holes 48E7 of the plates 42 and 44 and flows towards the plate 44. The refrigerant flows through a connecting tube 56e connected near the plate 44 and enters a tube 46 received in the holes 48D8 of the plates 42 and 44 and flows towards the plate 42. The refrigerant flows through a connecting tube 56f connected near the plate 42 and enters a tube 46 received in the holes 48E9 of the plates 42 and 44 and flows towards the plate 44. The refrigerant flows through a connecting tube 56g connected near the plate 44 and enters a tube 46 received in the holes 48D10 of the plates 42 and 44 and flows towards the plate 42. The refrigerant then flows through a connecting tube 56h connected near the plate 42 and enters a tube received in the holes 48F10 of the plates 42 and 44 and flows towards the plate 44.
As the refrigerant flows through the heat exchanger section of the first reheat circuit of the heat exchanger 22 from the outlet side 60 to the inlet side 62, the refrigerant is heated. The heated refrigerant then flows through a jumper 56i that flows the refrigerant to a reheat tube 66 (shown in
In the second reheat circuit, the refrigerant generally flows back and forth between rows H and I. As the refrigerant flows through the second reheat circuit, the refrigerant moves from the outlet side 60 of the heat exchanger 22 to the inlet side 62 of the heat exchanger 22.
The refrigerant enters the heat exchanger 22 at 52 and flows through a tube 46 received in the holes 48H2 of the plates 42 and 44. The refrigerant flows through a connecting tube 58a connected near the plate 44 and enters a tube 46 received in the holes 48H4 of the plates 42 and 44 and flows towards the plate 42. The refrigerant flows through a connecting tube 58b connected near the plate 42 and enters a tube 46 received in the holes 4815 of the plates 42 and 44 and flows towards the plate 44. The refrigerant flows through a connecting tube 58c connected near the plate 44 and enters a tube 46 received in the holes 48H6 of the plates 42 and 44 and flows towards the plate 42. The refrigerant flows through a connecting tube 58d connected near the plate 42 and enters a tube 46 received in the holes 4817 of the plates 42 and 44 and flows towards the plate 44. The refrigerant flows through a connecting tube 58e connected near the plate 44 and enters a tube 46 received in the holes 48H8 of the plates 42 and 44 and flows towards the plate 42. The refrigerant flows through a connecting tube 58f connected near the plate 42 and enters a tube 46 received in the holes 4819 of the plates 42 and 44 and flows towards the plate 44. The refrigerant flows through a connecting tube 58g connected near the plate 44 and enters a tube 46 received in the holes 48J10 of the plates 42 and 44 and flows towards the plate 42. The refrigerant then flows through a connecting tube 58h connected near the plate 42 and enters a tube 46received in the holes 48H10 of the plates 42 and 44 and flows towards the plate 44.
As the refrigerant flows through the heat exchanger section of the second reheat circuit of the heat exchanger 22 from the outlet side 60 to the inlet side 62, the refrigerant is heated. The heated refrigerant then flows through a jumper 58i that flows the refrigerant to a reheat tube 68 (shown in
As the refrigerant flows through the heat exchanger 22 and travels in the tubes 46 from the outlet side 60 of the heat exchanger 22 to the inlet side 62 of the heat exchanger 22, the refrigerant is heated as it accepts heat from the air 64 and flows through the heat exchanger circuits and the heat exchanger section of the reheat circuits. When the refrigerant in the heat exchanger sections reaches the tubes 46 near the inlet side 62 of the heat exchanger 22, the refrigerant is the warmest as it has absorbed heat from the air 64 flowing through the heat exchanger 22. The refrigerant then travels through the jumpers 56i and 58i and flows through the reheat tubes 46 in the reheat section of the reheat circuit that are received in the holes 48A1 and 48B2.
When the air 64 passes over the reheat tubes 66 and 68 received in the holes 48A1 and 48B2 of the plates 42 and 44 that contains the higher temperature refrigerant, the air 64 is slightly warmed by the heated refrigerant before it exits the heat exchanger 22, increasing the dry bulb temperature the air 64 and lowering the relative humidity of the air 64. The lower relative humidity air 64 can thus have more capacity to remove any moisture that had been deposited inside the interior display volume 26, preventing localized condensation onto the merchandise surfaces when additional moisture is introduced. Therefore, the condensation absorption capability of the air 64 is improved. The additional refrigerant pass through the reheat tubes 66 and 68 increases the temperature of the refrigerant by approximately 0.5° F. or more. This small increase in refrigerant temperature increases the exit temperature of the air 64, reducing the relative humidity from 100% to approximately 94% or lower.
Different configurations of heat exchanger circuits and reheat circuits are possible. That is, the circuit configuration can be changed based on the required application.
The foregoing description is only exemplary of the principles of the invention. Many modifications and variations of the present invention are possible in light of the above teachings. The preferred embodiments of this invention have been disclosed, however, so that one of ordinary skill in the art would recognize that certain modifications would come within the scope of this invention. It is, therefore, to be understood that within the scope of the appended claims, the invention may be practiced otherwise than as specifically described. For that reason the following claims should be studied to determine the true scope and content of this invention.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/US2007/079853 | 9/28/2007 | WO | 00 | 2/26/2010 |
Publishing Document | Publishing Date | Country | Kind |
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WO2009/041976 | 4/2/2009 | WO | A |
Number | Name | Date | Kind |
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6382310 | Smith | May 2002 | B1 |
6612119 | Eber et al. | Sep 2003 | B2 |
7231778 | Rigney et al. | Jun 2007 | B2 |
7779898 | Morrison et al. | Aug 2010 | B2 |
Number | Date | Country |
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WO2007061420 | May 2007 | WO |
Entry |
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International Search Report and Written Opinion for International Application No. PCT/US2007/079853, mail date Mar. 24, 2008, 6 pages. |
Number | Date | Country | |
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20100236752 A1 | Sep 2010 | US |