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| United States Patent Application |
20060137854
|
| Kind Code
|
A1
|
|
Haglid; Klas C.
|
June 29, 2006
|
Heat exchanger
Abstract
The ventilating system includes evaporative cooling of the exhaust air
before it enters a heat exchanger to cool incoming fresh outside air. A
suction fan pulls exhaust air through the heat exchanger and, in
combination with a flow restrictor, reduces the pressure on the exhaust
air and augments the evaporative cooling. The use of a pusher fan to
force outside air through the heat exchanger ensures that any leakage in
the heat-exchanger results in outside air entering exhaust air and
minimizing the chances of contamination by leaking exhaust air into the
incoming fresh air.
| Inventors: |
Haglid; Klas C.; (Wyckoff, NJ)
|
| Correspondence Address:
|
Gregor N. Neff, Esq.;Kramer Levin Naftalis & Frankel LLP
1177 Avenue of the Americas
New York
NY
10036
US
|
| Assignee: |
Building Performance Equipment, Inc. (a Delaware Corporation)
Wilmington
DE
|
| Serial No.:
|
321243 |
| Series Code:
|
11
|
| Filed:
|
December 29, 2005 |
| Current U.S. Class: |
165/54; 62/91 |
| Class at Publication: |
165/054; 062/091 |
| International Class: |
F24H 3/02 20060101 F24H003/02 |
Claims
1. A method of ventilating an enclosed space using an air handling system
including an isolating heat exchanger for conducting exhaust air form
said enclosed space and outside air into said enclosed space and
exchanging heat between said exhaust air and said outside air while
isolating the flows of said outside and exhaust air form one another, a
first fan to move said exhaust air through said heat exchanger, a second
fan to move said outside air through said heat exchanger, said first fan
being located downstream from said heat exchanger in the flow path of
said exhaust air for pulling said exhaust air out of said heat exchanger,
the steps of: (a) evporatively cooling said exhaust air at a cooling
location upstream of said heat exchanger in said flow path of said
exhaust air, and (b) creating a substantial air pressure drop between
said first fan and said cooling location to augment said evaporative
cooling.
2. A method as in claim 1 in which said creating step includes providing a
restriction to the flow of said exhaust air through said heat exchanger.
3. A method as in claim 2 in which said restriction comprises a member
made of porous material at least partially blocking the flow of said
exhaust air into said heat exchanger, said evaporative cooling step
including supplying water to said member.
4. A method as in claim 1 in which said second fan is used to force said
outside air into said heat exchanger.
5. A method as in claim 2 in which said restriction comprises a damper
selectively operable to restrict the flow path for exhaust air entering
said heat exchanger.
6. A ventilator for ventilating an enclosed space, said ventilator
including: (a) an isolating heat exchanger for conducting exhaust air
from said enclosed space and outside air into said enclosed space, and
exchanging heat between said outside air and said exhaust air while
isolating the flow of said exhaust air and said outside air from one
another, (b) a first fan to move said exhaust air through said heat
exchanger in a first direction, and (c) a second fan to move said outside
air through said heat exchanger in a direction generally opposite to said
first direction, (d) said first fan being a suction fan located
downstream from said heat exchanger and being oriented to pull air
through said heat exchanger, (e) a flow restrictor positioned to restrict
flow or exhaust air through said heat exchanger and produce a substantial
pressure reduction in exhaust air flowing through said heat exchanger,
and (f) an evaporative cooling device for evaporatively cooling said
exhaust air flowing through said heat exchanger.
7. A ventilator as in claim 6 in which said flow restrictor is selected
from the group consisting of an adjustable damper and a water evaporation
mat positioned to at least partially restrict the flow of said exhaust
air into said heat exchanger, said mat being part of said evaporative
cooling device.
8. A ventilator as in claim 6 in which said evaporative cooling device
includes a water sprayer for spraying water into said exhaust air before
it enters said heat exchanger.
9. A ventilator as in claim 6 in which the air conduit surfaces of said
heat exchanger are made essentially of thermoplastic material.
10. A ventilator for ventilating an enclosed space, said ventilator
including: (a) an isolating heat exchanger for conducting exhaust air
from said enclosed space and outside air into said enclosed space, and
exchanging heat between said outside air and said exhaust air while
isolating the flow of said exhaust air and said outside air from one
another, (b) a first fan to move said exhaust air through said heat
exchanger in one direction, and (c) a second fan to move said outside air
through said heat exchanger in a direction transverse to said first
direction, (d) said first fan being a suction fan located downstream from
said heat exchanger and being oriented to pull air through said heat
exchanger, said second fan being positioned upstream from said heat
exchanger and being oriented to push said outside air through said heat
exchanger; and (e) a flow restrictor positioned to restrict the flow of
exhaust air thorough said heat exchanger and produce a substantial
pressure reduction in said exhaust air flowing through said heat
exchanger.
11-31. (canceled)
Description
[0001] This patent application is a division of patent application Ser.
No. 09/829,772, filed Apr. 10, 2001, which is a continuation-in-part of
U.S. patent application Ser. No. 09/188,729, filed Nov. 9, 1998, new U.S.
Pat. No. 6,176,305, and Ser. No. 09/579,739 filed May 26, 2000.
[0002] This invention relates to ventilating systems and methods using
heat-exchangers for energy recovery, and to heat exchangers especially
exchangers suitable for use in such systems, and to methods for
fabricating heat exchangers.
[0003] The ventilating systems of the above-identified patent applications
represent significant improvements over prior ventilating systems.
Nonetheless, further improvements are desirable, and it is an object of
this invention to provide them.
[0004] One embodiment of the ventilating system of the above patent
applications uses evaporative cooling to cool exhaust air exiting a
building or other conditioned space. Although the evaporative cooling
feature significantly enhances the efficiency of cooling the conditioned
space, even greater cooling is highly desirable, as long as power and
equipment costs are not increased excessively.
[0005] Prior energy-recovery ventilating systems and others using
isolating heat-exchangers, that is, heat-exchangers which isolate the gas
flows from one another, often suffer from the effects of leakage in the
heat exchanger. This leakage causes undesired mixing of the two gases
from one another. In a ventilating system, this can mean that the stale
exhaust air mixes with the incoming fresh air, and leads to reduced air
quality and even contamination of the incoming fresh air.
[0006] A third problem occurs with the preferred heat exchanger used in my
above-described prior system. That heat-exchanger is made out of extruded
thermoplastic panels composed of side-by-side plastic tubes. The
heat-exchanger is admirably suited to use with evaporative cooling
equipment because mold and other such nemeses do not adhere strongly to
the heat-exchanger surfaces, and can be removed relatively easily. Also,
the heat-exchanger is relatively inexpensive to build and lasts much
longer than most metallic heat-exchangers.
[0007] A problem with such heat-exchangers is that most are relatively
less efficient in the transfer of heat than they could be.
[0008] Another problem is that such prior heat-exchangers usually require
relatively expensive housings, often made of sheet-metal.
[0009] A further problem is that such prior heat-exchangers usually are
assembled using hand labor, and thus are more time-consuming and
expensive to make than they need be.
[0010] In accordance with the present invention, the foregoing problems
are solved or alleviated by the provisions of a ventilating system and
method which includes evaporative cooling of the exhaust air before it
enters a heat exchanger to cool incoming fresh outside air. A suction fan
pulls exhaust air through the heat exchanger and, in combination with a
flow restrictor, reduces the pressure on the exhaust air and augments the
evaporative cooling.
[0011] Preferably, another fan is used to push outside air through the
heat-exchanger and into the conditioned space.
[0012] The use of a pusher fan to force outside air through the heat
exchanger ensures that any leakage in the heat-exchanger results in
outside air entering exhaust air and minimizing the chances of
contamination by leaking exhaust air into the incoming fresh air.
[0013] The heat exchanger is made economically by die-forming cavities in
relatively thick thermo-plastic sheets, interleaving them with other
thermo-plastic sheets having separate gas flow conduit structures, and
securing the sheets together. Preferably, the heat-exchanger is an
opposed-flow heat-exchanger giving improved heat-transfer efficiency.
[0014] In one embodiment, some or all of the sheets are panels of
parallel, side-by-side thermoplastic tubes.
[0015] In one specific embodiment, the tubes in every other sheet are left
intact and serve as conduits for one gas, such as outside air, while the
other sheets are indented to form separate conduits for another gas, such
as exhaust air.
[0016] In another specific embodiment, the sheets indented to form gas
flow passages are panels made of expanded thermoplastic materials.
[0017] In a further specific embodiment, all of the panels have gas flow
conduits formed by indenting the sheets.
[0018] Preferably, the outside edges of the sheets stacked together are
hot-compressed, with a heated roller, e.g. to melt the plastic of the
edges to form a relatively thick outer wall which is strong and helps
avoid the cost of a metal housing for the heat-exchanger. Flame singeing
is used to fuse the ends of gas flow conduits together.
[0019] The sheets are secured together, broad-face to broad-face, either
with silicone adhesive, or preferably, by heat-singeing at least one
broad surface of one of the sheets to make it tacky before another sheet
is pressed against the tacky surface to adhere the sheets together.
[0020] Vanes are die-formed in some of the gas flow passages to increase
turbulence and heat-transfer efficiency.
[0021] Die forming can be done with heated or cool dies, depending upon
the type of panel being used and its condition whether
hot and soft or
cool and hard, for example.
[0022] The foregoing and other objects and advantages of the invention
will be set forth in or apparent from the following description and
drawings.
[0023] FIG. 1 is a perspective view of a heat-exchanger constructed in
accordance with the present invention;
[0024] FIGS. 2, 3 and 4 are side-elevation views of sheets or panels used
to make the heat-exchanger of FIG. 1;
[0025] FIGS. 5, 6, and 7 are cross-sectional views, partially broken-away,
showing plural adjacent panels of heat-exchangers using the panels of
FIGS. 2, 3 and 4, and are taken at the locations indicated by the lines
5-5 , 6-6 and 7-7, respectively;
[0026] FIGS. 8, 9, 10 and 11 are perspective and cross-sectional
partially-schematic views illustrating equipment and steps used in the
manufacture of the heat-exchanger of FIG. 1; FIG. 12 is an elevation
view, partially schematic, showing a ventilating system of the present
invention; and
[0027] FIG. 13 is a cross-sectional view of a portion of an alternative
panel used in the invention.
HEAT EXCHANGER
[0028] FIG. 1 is a perspective view of one embodiment of the
heat-exchanger 20 of the present invention.
[0029] The heat-exchanger 20 has opposed broad side walls 22, and top and
bottom walls 24 and 26.
[0030] The heat-exchanger has an upper angular extension 28 defining an
upper inlet/outlet 30, and a lower angular extension 32 defining a lower
inlet/outlet 34 connected internally to the upper inlet/outlet 30. The
inlet/outlets 30 and 34 and the internal passageways (not visible in FIG.
1) interconnecting them form a first gas flow conduit.
[0031] A second gas flow conduit is formed by inlet/outlets 36 and 38 at
the right and left ends of the heat-exchanger, and internal passageways
(not visible in FIG. 1) interconnecting them.
[0032] Each of the various inlet/outlets 30, 34, 36 and 38 is capable of
being used either as an inlet or outlet for the flow of gases through the
heat-exchanger.
[0033] As it will be explained in detail below, the two gas flow conduits
are constructed to be parallel to one another over a substantial portion
of their lengths so as to produce counter-flow heat exchange when the
gases flow in opposite directions.
PANEL CONSTRUCTION
[0034] The heat-exchanger 20 is made of a plurality of vertical panels or
sheets 40, 42 interleaved with and secured to one another preferably in
alternating sequence.
[0035] FIG. 2 is a side elevation view of one of the panels 40, and FIG. 3
is a similar view of one of the panels 42.
[0036] The panels 40 and 42 are cut to have relatively long, straight
parallel upper and lower edges with upper and lower angular extensions 44
and 46, and 63 and 65, respectively. The extensions are of the same size
and shape so as to form the extensions 28 and 32 (FIG. 1) when the panels
are assembled together.
[0037] Preferably, both panels 40 and 42 are made of "sign-board"
material, whose construction is shown in cross-section in FIG. 5.
[0038] As it is shown in FIG. 5, each panel 40 has relatively thin opposed
outside walls 54 and 56 with broad surfaces, and elongated integral tubes
53 of rectangular or square cross-section formed between two walls 54 and
56. The panels are believed to be extruded from a thermoplastic material
such as polypropylene, polyethylene or polystyrene. Sign-board material
typically is used as relatively lightweight, strong and inexpensive
material for making signs or displays.
[0039] The structure of each panel 42 is substantially the same as the
structure of panel 40, and consists of outside walls 45 and 47 and tubes
43. The panels may be thicker than panels 40, and the tubes 43 larger in
cross-sectional area than the tubes 52, so as to facilitate the flow
conduit formation process.
[0040] As it is shown in FIGS. 3 and 5, the broad surfaces 45 and 47 of
each panel 42 are indented in selected areas to form a pair of gas flow
cavities 66. Preferably, the indentations are made by means of dies such
as the dies 136 and 138 shown in FIG. 11. The dies preferably are heated
in order to permanently deform the panel material.
[0041] When the panels 40 and 42 and assembled together with broad
surfaces contacting one another, as shown in FIG. 5, gas flow passageways
or conduits 67 and 69 are formed. Heat is transferred between the gas in
conduits 67 and 69 and a single-thickness wall 56 of each adjacent panel
40. This is an advantage over prior heat exchangers in which heat is
transferred through multiple wall thicknesses.
[0042] As it is shown in FIG. 5, the indentations compress the internal
walls of the tubes together to form a two-ply wall 84 in the center of
the panel 42, with ribs 86 extending outwardly at the locations of the
compressed internal walls.
[0043] Preferably, vanes 76 (see FIG. 3) are formed in the gas flow
cavities 66 by the provision of cavities in the dies 13 and 138 (FIG.
11), which has the effect of leaving the panel material uncompressed and
projecting outwardly from the two-ply wall 84. The vanes 76 are arranged
to serve as baffles to ensure the turbulent flow of gas along sinuous
paths 80 through the conduits 67 and 69, thus increasing the heat
transfer efficiency of the heat-exchanger.
[0044] Optional guide and support vanes 82 and 83 (FIG. 3) are formed by
the same process as the vanes 76 to divide the inlet section of each
cavity 66 into the passageways 72 and 74. The vanes 82 and 83 help to
direct the flow of air through the conduits 67 and 69 first horizontally,
from right to left, as shown in FIG. 3, and then outwardly and downwardly
through the outlet passageways 72 and 74.
[0045] The vanes 72, 74, 76, 82 and 83 also help to support the adjacent
portions of panels 40 to maintain a constant spacing of the panels from
one another over the relatively broad span of the inlet and outlet
openings.
[0046] An alternative panel construction 88 is shown in FIG. 4.
[0047] Panel 88 is an alternative to the panel 40 for conducting the gas
flow from one end 38 (FIG. 1) to the opposite end 36.
[0048] Panel 88 has one or more indentations 94 with vanes 96, 102 and 104
formed by the same process as the vanes 76. The dashed lines 97 indicate
the locations of rows of added vanes 96, which are not shown in FIG. 4
for the sake of simplification of the drawings.
[0049] The vanes 102 and 104 are provided in order to support the adjacent
panels in the heat-exchanger, and to guide gases into and out of the flow
passages of the heat-exchanger.
[0050] FIG. 7 shows the cross-sectional shape of one of the vanes 96.
[0051] The advantage of the panel 88 over the panel 40 is that the gas
flow through the conduits is turbulent, thus further increasing the
heat-transfer efficiency of the heat-exchanger.
[0052] Although it is preferred that the gas flow cavities in the panels
be formed by indenting both broad side walls of the panels to form a
central two-ply web 84 as shown in FIG. 5, alternatively, the panels can
be indented from only one side to form the gas flow cavity 94.
[0053] FIG. 6 is a cross-sectional view taken along line 6-6 of FIG. 4
showing this alternative construction. The panel which is indented has
broad side walls 54 and 56 with tubes 52. The panel is heat-compressed to
form a gas flow passageway in the area 112, and a two-ply wall 113 with
ridges 114 at the locations of the compressed inner walls.
[0054] Heat is transferred between the gas in the conduit 112 and that
flowing in the tubes 52 of the adjacent panels 40. Although heat is
transferred through only one wall thickness in the case of the wall 56,
heat must flow through the two-ply wall 113 and wall 54, when being
transferred between conduit 112 and the right-hand panel conduits 52
shown in FIG. 6.
[0055] This potential reduction in heat transfer efficiency, as compared
with the FIG. 5 embodiment, can be acceptable as a compromise to avoid
having to make two sets of heat-forming dies or heat-forming both sides
of the panels in separate steps using the same dies, if the extra die
cost is avoided by using the same dies to form both sides of one panel.
[0056] The heat transfer reduction can be minimized by reducing the
internal and external wall thickness of the panels 88, and by removing
substantial sections of the two-ply wall 113 at many locations (e.g.
115--see FIG. 4), in the panel shaping process.
[0057] The panels 40 utilize the tubes 52, which extend the whole length
of the panel, as gas flow conduits. However, the panels 42 and 88 do not
use the tubes to conduct gas. Instead, the panels are merely used as
low-cost thermoplastic sheet material from which to form gas flow
conduits. It is possible to use other sheet materials instead for the
starting sheets for forming the panels 42 and 88.
[0058] For example, it is believed that sheets of expanded thermoplastic
materials, such as polypropylene, polyethylene or polystyrene can be used
instead of the "sign-board" material. Such sheet materials are widely
used as insulating panels in home construction, as flotation materials
for floating docks, etc.
[0059] FIG. 13 is a broken-away cross-section of a panel of expanded
thermoplastic material 117 compressed at 119 to form gas flow cavities
121 and 123. This construction can be easier and less expensive to make
than that using sign-board as the starting material for all panels.
[0060] Similarly, other compressible and/or heat-formable sheets may be
advantageous to use as starting materials. For example, expanded or solid
thermo-plastic sheets, still
hot after being formed, can be stamped or
molded rapidly to provide the desired gas flow cavities without the
heating of dies. Some materials may be subject to permanent deformation
by the use of cool dies alone. It also is within the scope of the
invention to use those materials as alternatives.
ASSEMBLY OF PANELS
[0061] The next step in making the heat-exchanger 20 after cutting and
forming the panels is to adhere the panels together, with broad surfaces
contacting one another, in alternating sequence. That is, for example, a
panel 40 forms one side wall 22 of the heat-exchanger, and a panel 42 is
secured to it. The next panel is another panel 40, the next is another
panel 42, etc. The other side wall 22 of the heat-exchanger would be
another panel 40.
[0062] The panels are adhered to one another with silicone adhesive, or by
use of the process partially illustrated in FIG. 10.
[0063] Referring to FIG. 10, several flaming jets 124 are pointed
downwardly from burner nozzles 126 fed with fuel (e.g., natural gas) from
a manifold 132. The flames are played onto the upper surface of one of
the panels 40 while the panel is moved past the flames in the direction
134 at a controlled speed so as to "singe" the upper surface 56 of the
panel 40. This slightly melts or softens the upper surface of the panel.
Then, the next panel is placed on top of the first panel, either with or
without singeing the surface which is to make contact with the first
panel, and the panels are pressed together and allowed to cool to cause
them to adhere.
[0064] This process then is repeated for each subsequent panel added to
the stack until a pre-determined number of layers has been formed.
[0065] The panels can be held together by many other methods and
structures.
[0066] For example, metal clamps can be formed out of metal angles and
cross rods (not shown) clamping the panels together.
[0067] Another assembly method which is believed to be feasible, under
some circumstances, is to simply clamp the panels together temporarily
until the edges of the panels are fused together, in the manner to be
described below, and then removing the clamps, with the fused edges being
sufficient to hold the panels together.
EDGE FUSING
[0068] FIG. 8 shows the preferred method of forming the top and bottom
walls 24 and 26.
[0069] When the panels are stacked together, the edges are aligned with
one another to form straight surfaces. Then, a heated roller 118 is
pressed firmly against the upper edges 116 of the panels while the panels
are moved as indicated by the arrow 120. This progressively compresses
and melts the upper edges of the panels, and the melted plastic is rolled
by the roller to form a solid wall of melted plastic.
[0070] The panels then are turned over to use the same process to form the
opposite wall.
[0071] Alternatively, a second heated roller (not shown), spaced
vertically from the roller 188 can be used simultaneously to form the top
and bottom walls in one pass of the panels through the heated roller
mechanism.
[0072] Many types of heated rollers can be used, such as
ultrasonically-heated rollers or rollers heated with electrical
resistance heating.
[0073] The edges of the panels at the four inlet/outlets 30, 34, 36 and 38
(FIG. 1) are fused together by flame singeing, as shown in FIG. 9,
without closing or significantly reducing the size of the gas
inlet/outlet openings.
[0074] A flame array like that shown in perspective view in FIG. 12 is
used. The array is shown in FIG. 9 in a side elevation view to show the
features of each flame 124.
[0075] The flame 124 is a jet of burning gas moving downwardly in the
direction of the arrows 128. The position and thrust of the jet are
adjusted so that just the bottom portion of the flame touches the upper
edges 122 of the panel assembly as the assembly is moved past the flame
array in the direction of the arrow.
[0076] The dwell time of the flames on the panel edges is controlled
empirically to limit the melting of the panel end to just enough to fuse
the adjacent panel ends together without significantly closing the gas
passageways in the panels.
[0077] Other means can be used to fuse the ends and edges of the panels
together, such as heated rollers and like devices.
[0078] The fused top and bottom walls 24 and 26, and the fused edges of
the panels at the inlet/outlet locations produce a strong heat-exchanger
structure which is capable of supporting itself without a separate
housing, thus saving substantial costs for sheet metal and sheet metal
fabrication as compared with comparable prior heat-exchangers.
[0079] The heat-exchanger 20 is weather-resistant, highly
corrosion-resistant, relatively easy to keep clean, and efficient, as
well as being relatively economical to make.
VENTILATION SYSTEM
[0080] FIG. 12 is a partially-schematic side-elevation view of a
ventilation system utilizing the heat-exchanger 20 of the invention to
ventilate a building or other conditioned space 160.
[0081] As in my U.S. Pat. No. 6,176,305, a first fan 144 is positioned at
the left inlet end 38 of the heat-exchanger to push outside air ("OSA")
through the heat-exchanger and out of the outlet 36 and into the
conditioned space 160.
[0082] The outside air flows as indicated by the arrows 146 and 148
through an opening 149 in the wall 151 of a building and a fitting 147
secured to the left end of the heat-exchanger, and out through another
fitting 153 secured to the right end of the heat-exchanger.
[0083] Curved fittings 154 and 156 fit over the angular extensions 28 and
32 of the heat-exchanger.
[0084] Mounted inside of outlet fitting 156 is a duct fan 142 which acts
as a suction fan to pull exhaust air thorough inlet duct 154 and the
heat-exchanger and expel the air through an exhaust outlet 155.
[0085] At the exhaust inlet end of the heat-exchanger is a motorized
damper 152, a water spray nozzle 150, and a porous mat 158 onto which the
spray nozzle 150 sprays water to create evaporative cooling of the
exhaust air, when needed.
[0086] In accordance with the present invention, either the fiberglass mat
158 or the damper 152, or a combination of both is used to create a
restriction to the inflow of exhaust air into the heat-exchanger.
[0087] Use of the damper 152 is preferred so as to minimize the
restriction caused by the mat 158, especially when evaporative cooling is
not required.
[0088] The exhaust fan 142 preferably is a centrifugal duct fan which
occupies the full width of the duct 156 and is capable of creating a
substantial pressure drop. The combination of this suction fan with the
flow restriction creates a significant pressure drop in the exhaust air
entering the heat-exchanger. This is believed to significantly increase
the evaporation of water and, hence, the evaporative cooling of the
exhaust air.
[0089] Another advantage of this ventilating system is that it provides
resistance to the leakage of exhaust air into the incoming fresh air
through any leaks which may exist in the heat-exchanger. This is because
the exhaust air in the heat-exchanger is at a lower pressure than the
outside air, and any leaks would allow flow from the higher pressure
conduits to the low pressure conduits, but not in the opposite direction.
[0090] Thus, stale air is not allowed to mix to any significant degree
with the fresh air coming into the conditioned space. Although this is
highly desirable in any residential or commercial building, it is
especially advantageous in hospitals or doctor's offices where it is
important to prevent such mixing in order to prevent the spreading of
pathogens.
[0091] Preferably, the heat-exchanger 20 is mounted with the right end
slightly higher than the left so that the body of the heat-exchanger
forms an angle .PHI. of around 5 degrees with horizontal. This promotes
drainage of condensate and excess water from the evaporative cooling
system towards the left end 38
[0092] A gutter 162 is provided in the duct 156 to catch the water
draining from the exhaust passageways of the heat-exchanger. The water
gathered there flows through a line 168 to an optional waste water
recovery facility (not shown) which returns the water for re-use in
evaporative cooling, or elsewhere.
[0093] A float valve 164 is provided. It closes the drain system until the
water level in the tank of the valve 164 reaches a level sufficient to
overcome the negative pressure of the fan 142. This prevents the drain
from leaking air into the fitting 156 and reducing the effectiveness of
the fan.
[0094] A similar gutter 166 and drain 170 are provided at the right end of
the heat-exchanger, if needed. A similar gutter and drain can be provided
at the left end of the heat-exchanger, if needed.
[0095] The system shown in FIG. 12 preferably also has suitable control
means for controlling the operation of the ventilator in heating, cooling
and intermediate cooling modes, as described in my above-identified
patent and pending patent application. Louvers, bypass ducts, de-icing
means, etc., described there all can be used in the system of FIG. 12, as
needed or desired.
[0096] The above description of the invention is intended to be
illustrative and not limiting. Various changes or modifications in the
embodiments described may occur to those skilled in the art. These can be
made without departing from the spirit or scope of the invention.
* * * * *