Method and apparatus for dew point evaporative product cooling

• US 6,776,001 B2
• Filed: 10/28/2002
• Issued: 08/17/2004
• Est. Priority Date: 02/07/2000
• Status: Expired due to Term

• Current Assignee: FF Seeley Nominees Pty Ltd.
• Original Assignee: Idalex Technologies, Inc.
• Inventors: Gillan, Alan D., Gillan, Leland E., Maisotsenko, Valeriy, Heaton, Timothy L.
• Primary Examiner(s): Jiang, Chen Wen
• Application Number:
  US10/203,195
• Publication Number:
  US 20030126876A1
• Time in Patent Office: 659 Days
• Field of Search: 623/15, 623/14, 623/04, 623/10, 621/21, 621/71, 62/91, 261/153, 261/154
• US Class Current: 62/315
• CPC Class Codes: F24F 1/0007 Indoor units, e.g. fan coil units self-contained units F24F1/02
• CPC Class Codes: F24F 1/0059 characterised by heat exchangers
• CPC Class Codes: F24F 2203/1032 Desiccant wheel
• CPC Class Codes: F24F 2203/1064 Gas fired reheater
• CPC Class Codes: F24F 2203/1068 comprising one rotor
• CPC Class Codes: F24F 2203/1084 comprising two flow rotor segments
• CPC Class Codes: F24F 3/1423 with a moving bed of solid desiccants, e.g. a rotary wheel supporting solid desiccants
• CPC Class Codes: F24F 5/0035 using evaporation
• CPC Class Codes: F28D 5/00 Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, using the cooling effect of natural or forced evaporation
• CPC Class Codes: F28D 5/02 in which the evaporating medium flows in a continuous film or trickles freely over the conduits
• CPC Class Codes: Y02B 30/54 Free-cooling systems

Abstract

The present invention relates to a method and an apparatus for providing enhanced indirect evaporative cooling of air, water, fuel, or other fluids while controlling the humidity. The design makes cooling down to the dew point possible without energy input other than the energy to produce the fluid flow needed. The design makes use of stacked composite plates (7) with channels (1, 2) for fluid flow between adjacent plates. On opposing surface areas of these plates, there are wet areas (4) or dry areas (3). The wet areas (4) provide cooling by conventional evaporation which is in turn used to cool the fluids in contact with the dry areas (3). The benefit is controlled heat transfer, which allows selected cooling of fluid flow such that the temperature as low as dew point are reachable.

Claims

1. A method to provide indirect evaporative cooling while controlling humidity of the cooled product air by having three plates in parallel:

a) forming a first space and second space between adjacent plates with the middle plate being a common plate to both spaces;

b) wetting opposing surfaces of the adjacent plates;

c) keeping some surface areas of opposing surfaces dry;

d) passing air in the first space in two types of channels, working channels and product channels;

e) passing air in the second space in working channels and product channels in cross flow to the flow in the first space channels;

f) controlling the humidity in the product channels by the amount of wet surfaces the product air is exposed to in the product channels; and

g) cooling the air in the product channels by the dry surfaces being cooled by heat transfer across the common plate in this area and the evaporation cooling on the opposite surface of the common plate in the adjoining space that is occurring in a wet area of a working channel.

2. The method of claim 1 wherein pre-cooling occurs in each space in a section where working channels are on both sides of the common plate having dry areas and wet areas having equal area;

the pre-cooling section having the dry area occurring first in the working channel having the transitive to a wet area occurring on a diagonal to the direction of flow in the working channel having the orientation of the working channel dry area in a first spacing being opposite from the dry area of the working channel of the second space such that the common plate dry area in the first space is opposite the wet area of the common plate in the second space pre-cooling of the working air in the second space by heat transfer from the first space and pre-cooling of the working air in the first space by heat transfer from the second space.

3. A method according to claim 1 wherein after the product fluid, for example air, has passed through the product cooling section it passes over a wet surface.

4. A method according to claim 1 wherein the product fluid includes its own fluid moving device.

5. A method according to claim 1 wherein the working air is heated before entering the pre-cooling section.

6. A method according to claim 1 wherein the humid working air exhaust becomes the product and is directed to the user for humidification of desired area.

7. A method according to claim 1 wherein outside ventilation air is used as the product fluid for the user in, for example, a conditioned space and is passed through a solid or liquid desiccant dehumidifier, and this product air is then cooled by passing its two streams over the dry side of two product cooling sections, and then is directed to the user;

and simultaneously at least one of either the exhaust air from conditioned space and/or outside air that has passed through a solid or liquid desiccant humidifier is used as the working air, that then passes by two streams through the pre-cooling section, is then directed straight across the product cooling section and then is exhausted out.

8. A method according to claim 1 wherein all or a portion of the inside recirculation air is used as a product fluid for the user in, for example, a conditioned space and is passed through a solid or liquid desiccant dehumidifier;

this product air is cooled by passing its two streams over the dry side of two product cooling sections and then is directed to the user;

simultaneously outside air and in some case all or a portion of the same recirculation air from conditioned space, after its passing through the desiccant dehumidifier, is used as the working air, that then passes by two streams through the pre-cooling section, is directed straight across the product cooling section and then is exhausted out.

9. Apparatus for indirect evaporative cooling comprising:

at least two plates in parallel, each plate having two surfaces, and wherein

a) at least part of one of the surfaces is impermeable to the fluid used for evaporation,

b) the plates are made of a material that has a wick like capability that transports the liquid used for evaporation to the areas of the plates where evaporation is to occur and once there allows the liquid to evaporate,

c) the impermeable areas are thin, so as to allow for heat transfer,

d) the opposing surfaces of adjoining plates are of like surface permeability,

e) the evaporation occurs in the areas without the impermeable surface and cools the surface and the working air,

f) the cooler temperatures due to the evaporation is in heat transfer contact with the impermeable surface and the product air that is in contact with this surface, and

g) the apparatus has channel guides, working air channels, and product air channels to direct the flow in a desired path.

10. The apparatus of claim 9 wherein the plate shape is of a diamond.

11. The apparatus of claim 9 wherein the plate shape is square.

12. The apparatus of claim 9 wherein the impermeable surface is created by a plastic coating on the wick material.

13. The apparatus of claim 9 where the plates of the stack have impermeable surfaces on the product channels to inhibit any direct evaporation occurring.

14. The apparatus of claim 9 where the working channels have some areas of impermeable surface.

15. The apparatus of claim 9 where the plate shape has one part removed.

16. The apparatus of claim 9 where the plate shape uses the fourth quadrant to have direct evaporative cooling of the product air after it has been cooled by the indirect cooling.

17. The apparatus of claim 9 where the plates are fed the liquid for evaporation by feeder wicks.

18. The apparatus of claim 9 where the plates are sloped with the lower edge fed liquid for evaporation by a reservoir.

19. The apparatus of claim 9 where the working air is heated before it is used in the working air channels.

20. The apparatus of claim 9 where the working air is dehumidified before it is used in the working air channels.

21. The apparatus of claim 9 where flow of working air and product air between adjoining channels separated by a plate are in cross flow.

22. The apparatus of claim 9 where flow of working air and product air between adjoining channels separated by a plate are more counterflow.

23. The apparatus of claim 9 where the working air is taken from the exhaust after the product air was used.

24. The apparatus of claim 9 where some working air exhaust is added to the product air to accomplish the desired temperature and humidity.

25. The apparatus of claim 9 wherein:

a) one of the quadrants with only working air channels has one half of each quadrant surface covered with plastic, such that the working air enters one channel;

b) the channel is in the non evaporative portion of the channel and gets pre-cooled by adjacent layers;

c) the working air channels also in the quadrant have evaporative cooling in area of their channels; and

d) the channels interface with the first channel plastic surface.

26. A method to provide indirect evaporative cooling and to control the humidity by having at least two plates with two surfaces wherein there is:

a) wetting on opposite surfaces of the two plates;

b) keeping some surfaces areas of the opposing surfaces dry;

c) passing air between the plates;

d) controlling the humidity by varying the amount of wet surfaces to which the air is exposed; and

e) cooling the air over the dry areas by heat transfer by having evaporation occurring on the opposite side of each plate in the area.