U.S. patent number 3,731,461 [Application Number 05/026,317] was granted by the patent office on 1973-05-08 for drift eliminators for atmospheric cooling tower.
This patent grant is currently assigned to Societe Hamon Sobelco S.A.. Invention is credited to Maurice Hamon.
United States Patent |
3,731,461 |
Hamon |
May 8, 1973 |
DRIFT ELIMINATORS FOR ATMOSPHERIC COOLING TOWER
Abstract
To reduce or eliminate droplet formation in the plume issuing
from a cooling tower, a layer of finned tubes is provided to heat
the moist air prior to its issuance from the tower. The fins have a
shape similar to conventional drift eliminator blades and thus the
blades, at the same time, function to eliminate droplets from the
gas stream. In addition, the above-mentioned tubes can be fitted
with vertical outlet tubes or nozzles such that the finned tubes
fulfill the following functions: Collect the water droplets
contained in the air leaving the cooling tower; Warm up the air
leaving the tower; and Distribute the water to be cooled in the
cooling tower, over the heat transfer section.
Inventors: |
Hamon; Maurice (Brussels,
BE) |
Assignee: |
Societe Hamon Sobelco S.A.
(Brussels, BE)
|
Family
ID: |
21831137 |
Appl.
No.: |
05/026,317 |
Filed: |
April 7, 1970 |
Current U.S.
Class: |
96/356;
261/DIG.11; 261/DIG.77; 261/111; 261/117; 261/158 |
Current CPC
Class: |
F28C
1/14 (20130101); Y02B 30/70 (20130101); Y10S
261/11 (20130101); Y10S 261/77 (20130101) |
Current International
Class: |
F28C
1/14 (20060101); F28C 1/00 (20060101); B01d
045/06 () |
Field of
Search: |
;261/DIG.11,152,156,158,118,108,111,117 ;55/257,222,267-269,440,446
;165/181,182 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
Primary Examiner: Nozick; Bernard
Claims
I claim:
1. An atmospheric cooling tower comprising side walls provided with
an air inlet means for atmospheric air and having a top outlet
means for the exit of heated outlet air, gas liquid contact means
within the tower intermediate the air inlet means and the air
outlet means, a plurality of heat exchange tubes arranged in a
generally horizontal layer transversely within the tower above said
contact means, a plurality of metallic fins mounted on the tubes in
heat exchange relation therewith, said fins being in generally
parallel relation and being nonplanar and defining a series of
tortuous vertical flow paths for the heat exchange flow of the
outlet air over the tubes, means provided at the ends of the tubes
for passing through said tubes a heated liquid with the outlet air
passing from the contact means through the flow paths so as to
reduce liquid droplets suspended in the outlet air existing through
the outlet means and to reduce the relative humidity of said outlet
air, and said tubes having depending outlet nozzles for directing
the heated liquid therein onto the contact means within the cooling
tower.
2. The invention of claim 1 wherein the fins are spaced apart and
define zig-zag air flow passages.
3. The invention of claim 1 wherein the fins have upper end
portions through which the tubes pass so that the major portions of
the fins depend from the tubes.
4. The invention of claim 1 wherein the means at one of the ends of
the tubes is an outlet header means and is in fluid communication
with the water supply system for the tower.
5. The invention of claim 1 wherein the means at one of the ends of
the tubes is an inlet header means and is in communication with a
source of heated liquid.
Description
This invention relates to drift eliminators for cooling towers. In
general, a cooling tower is a device wherein an exchange of heat
takes place between a liquid such as water from a power plant
installation and atmospheric air. This liquid is allowed to play or
drip down from a plurality of nozzles or other outlet means through
a heat exchange grid within the cooling tower. The cooling towers
may be of a considerable vertical extent and are defined by
criss-crossed, for example, wooden boards, slats, or the like,
which define a plurality of contact surfaces to interrupt and
deflect the falling liquid and to bring about intimate contact
between the liquid and the cooling gas stream, generally air. The
cooling tower may be of the natural or of the induced draft type.
In an induced draft type, the hot water generally enters from the
top of the cooling tower and by the time it reaches the bottom has
experienced an appreciable temperature drop. The air as it exits
from the cooling tower will be at a higher temperature than the air
which enters the cooling tower because of the heat exchange with
the warm liquid.
The atmospheric natural draft or mechanical draft cooling towers
offer the drawback of giving generally a vapor plume at the outlet
of the hot air, which causes drizzle precipitation of droplets in
the neighborhood of the tower. Such precipitation is not desirable
for a variety of reasons; for example, droplets of water may freeze
on nearby roads in the winter thus creating a safety hazard.
Further, atmospheric pollution due to the precipitating droplets
collecting smoke and other impurities may take place.
Conventional drift eliminators normally provided in atmospheric
cooling towers above the heat transfer packing in the tower only
partially avoid the above-mentioned drawbacks. The failure of
conventional drift eliminators is primarily due to the fact that
the air issuing from the tower is saturated or close to its
saturation point and mixing of the warm saturated gas with the
cooler ambient atmosphere induces condensation and super-saturation
of the air in the vicinity of the gas distributed from the cooling
tower.
Conventional drift eliminators are generally constructed of metal,
plastic or asbestos cement and the blades or fins thereof are
shaped to cause a baffling of the air passing therebetween. The
baffling of the air often results in the failure of the fins or
blades to remove the smallest airborne droplets constituting the
fog or mist leaving the tower.
The present invention is directed to drift eliminators generally
consisting of one or more layers of metallic finned tubes, with the
fins being arranged similarly to the arrangement of fins in
conventional drift eliminators. The tubes associated with the fins
are fed by heated water directed to the cooling tower. The heated
fluid directed to the finned tubes is afterwards distributed by the
conventional hot water distribution system for the tower. Heat
transmitted by the finned tubes from the heated water to the air
passing through the tower increases the air's temperature without
increasing its actual vapor content. The forgoing results in a
decrease in the relative humidity of the air issuing from the tower
and consequently a substantial reduction or the complete
elimination of condensation of vapor at the outlet of the tower or
in the vicinity thereof. These favorable conditions are also
brought about by the fact that droplets of liquid which may not be
eliminated by the shaped fins of the drift eliminator are
evaporated by the warmed air in which the relative humidity has
been reduced by the heated water. Condensation nucluii formed by
liquid droplets which would normally issue from conventional
atmospheric cooling towers are thus eliminated or substantially
reduced.
In general, all of the heated water to be cooled is fed to the
finned tubes of the invention and after passing through the tubes
the water is directed to the normal water distribution system of
the cooling tower.
It is contemplated, however, that only a part of the hot water flow
to the tower may be directed to the finned tubes and after flowing
therethrough the water may be combined with the hot water being
directed to the normal distribution system of the cooling
tower.
A third situation may comprise passing a heated liquid, which is at
a temperature higher than the normal temperature of the air passing
from the tower, to the drift eliminator tubes in order to heat the
air and cool the liquid without direct contact between the liquid
and the atmosphere.
Further, the fluid directed to the finned tubes may comprise a
vapor which is condensed in the drift eliminator tubes.
The heated liquid or the vapor referred to above may be entirely
independent of the water to be cooled in the cooling tower.
The present invention may also comprise at least one layer of
horizontal finned tubes with each of the tubes being provided with
a series of downwardly directed bores or holes within which are
secured liquid distribution nozzles. With this form of construction
the system accomplishes the following:
removal of liquid droplets suspended in the air leaving the cooling
tower;
the distrbution of water to be cooled over the packing of the
cooling tower; and distribution
the reduction of the relative humidity of the air leaving the
cooling tower .
The invention will be more particularly described in reference to
the accompanying drawing wherein:
FIG. 1 is an elevational cross-section of a typical forced draft
cooling tower containing apparatus constructed in accordance with
the present invention.
FIG. 2 is a view of a typical prior art drift eliminator blade
construction.
FIG. 3 is a view of such a device modified to include the vapor
plume reducer according to the practice of this invention.
FIG. 4 is a perspective view of a portion of the vapor plume
reducing means illustrated in FIG. 3.
FIGS. 5, 6, 7 and 8 are cross-sectional views of embodiments
similar to that shown in FIG. 3.
FIG. 9 is a perspective view of a further modification of the
present invention.
Referring now to FIG. 1 of the drawing, 10 generally denotes a
cooling tower of the type often employed in conjunction with
air-conditioning systems and includes vertical walls 12 which rise
above the base 13. A plurality of apertures 14 are provided in the
lower portion of the walls 12 for the intake of atmospheric air. At
the upper end of the tower 10 is a warm, moist air exit shroud 16,
which ideally is of a Venturii type construction and adjacent the
throat of the Venturii is mounted an air moving fan means 18
connected to a suitable electric motor 20 via shaft 22 and speed
reducing gear means 24, which gear means is supported from a spider
26 mounted in the upper end of the tower.
Below the spider 26 and adjacent the exit orifice 16 is mounted the
improved vapor plume reducer 28 constructed in accordance with the
present invention as to be more fully described in reference to
FIGS. 3 through 8 of the drawing.
Below the vapor plume eliminator 28 are a plurality of headers 30,
each of which is provided with nozzled outlets 32 whereby the
liquid to be cooled is uniformly distributed downwardly onto an
array of vertically stacked, lathed, frame elements generally
designated 34, which in turn are supported by cross-beam members
36, as more fully described in U.S. Pat. application, Ser. No.
771,513, filed Oct. 29, 1968 for "Cooling Tower," A.A.A.
Lemmens.
Adjacent the bottom of the tower means 31 are provided to remove
the cooled liquid such as water from the tower.
FIG. 2 shows one of the more frequent realizations of conventional
drift eliminators. These drift eliminators 50 are made of a series
of blades 52 parallel-arranged at a short distance one from the
other and having such a shape that most of the droplets contained
in the air are collected because of its sinuous flow pattern
between those blades. The elements 54 are used to join the blades
together by maintaining them parallel and at a short distance one
from the other.
Referring to FIGS. 3 and 4, one form of the system of the present
invention is illustrated, which system consists of a plurality of
metallic blades 58 through which pass the tubes 56. The tubes 56
are fed by water entering the cooling tower or by an independent
hot water flow via, for example, header tube 60, illustrated in
FIG. 1 of the drawing. The fins 58 are intimately joined to the
tubes 56 and the assembly may be constructed, as is well known in
the art, by, for example, welding or force fitting the fins to the
tubes.
The specific shape of the fins is not critical and the fins and
tubes may be shaped as illustrated at 56 and 58' of FIG. 5; 56 and
58" of FIG. 6; 56 and 59 of FIG. 7; or 56 and 59' of FIG. 8.
Referring specifically to FIG. 8, this form of the invention offers
the advantage of a substantially better heat transfer between the
water flowing through the tubes 56 and the air passing about the
fins as the upper portion of the fins remains free or substantially
free of water droplets.
Referring specifically to FIG. 9, there is shown one of the
possible arrangements wherein the system fulfills simultaneously
all of the preferred functions, heretofore set forth; that is, the
retention of droplets contained in the air leaving the tower, the
reduction of the relative humidity of air, and finally, the
distribution of water to be cooled over the filling of the
tower.
Referring now to this FIG. 9 of the drawing, the numeral 70 denotes
generally a bank of parallel heat transfer finned tubes wherein
each individual fin element is denoted by the numeral 72 and each
tube is designated 74. Each tube or tube segment 74 is in turn
provided with downwardly depending tubes 76. The arrows coming in
from the right of the drawing illustrate hot water which is fed to
the cooling tower for treatment, which water heats the fins 72 as
described above and, in the present embodiment, the water is then
released from the tubes 74 through the outlet tubes 76 and falls or
flows downwardly onto the packing of the cooling tower for
conventional treatment.
Where desired a plurality of layers of finned tubes constructed in
accordance with the present invention may be arranged one above the
other adjacent the exit of a cooling tower. The tubes of each of
the layers may be connected to the same source or to different
sources of heating fluid and the flow circuit for the fluid may be
arranged in parallel, in series, or series parallel flow.
It is also contemplated that the finned tubes or mist eliminator of
the invention may be employed in conjunction with conventional mist
eliminators in stacked arrangement or the finned tube mist
eliminator of the invention may cover only a portion of the
cross-sectional area of the tower with the remaining area being
fitted with conventional mist eliminators.
It will also be apparent that when a plurality of stacked
eliminators are employed only the lowermost layer would be provided
with outlet tubes such as illustrated in FIG. 9 and further that
where outlet tubes or nozzles are employed, as illustrated in FIG.
9, the nozzles or outlets of the tubes have a length such that the
liquid issuing therefrom does not impinge on the fins or eliminator
blades.
* * * * *