U.S. patent application number 16/016631 was filed with the patent office on 2018-10-25 for method and apparatus for treating potable water in municipal and similar water tanks.
The applicant listed for this patent is Medora Environmental, Inc.. Invention is credited to Joel J. Bleth, Gary A. Kudrna, Corey M. Simnioniw, Willard R. Tormaschy, Douglas P. Walter, Jonathan L. Zent.
Application Number | 20180305224 16/016631 |
Document ID | / |
Family ID | 51293328 |
Filed Date | 2018-10-25 |
United States Patent
Application |
20180305224 |
Kind Code |
A1 |
Simnioniw; Corey M. ; et
al. |
October 25, 2018 |
METHOD AND APPARATUS FOR TREATING POTABLE WATER IN MUNICIPAL AND
SIMILAR WATER TANKS
Abstract
Method and apparatus for treating potable water in municipal and
similar tanks to reduce and remove undesirable disinfectant
byproducts such as trihalomethanes from the water by providing a
water circulation system to create circulation patterns in the tank
water and an air flow system for creating an air flow pattern in
the headspace region of the enclosed tank above the water surface.
In operation, a portion of the tank water is drawn-up a draft tube
from the tank floor to above the water surface and sprayed through
a nozzle outwardly about a vertical axis and slightly downwardly
toward the surface of remaining tank water. The air flow system
creates and directs a high volume of air through the tank above the
water surface to volatize undesirable trihalomethanes in the
drawn-up water portion to gaseous state to enter the air flow
pattern and exit the tank into ambient air.
Inventors: |
Simnioniw; Corey M.;
(Belfield, ND) ; Zent; Jonathan L.; (Dickinson,
ND) ; Tormaschy; Willard R.; (Dickinson, ND) ;
Bleth; Joel J.; (Dickinson, ND) ; Kudrna; Gary
A.; (Dickinson, ND) ; Walter; Douglas P.;
(Dickinson, ND) |
|
Applicant: |
Name |
City |
State |
Country |
Type |
Medora Environmental, Inc. |
Dickinson |
ND |
US |
|
|
Family ID: |
51293328 |
Appl. No.: |
16/016631 |
Filed: |
June 24, 2018 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
|
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13763379 |
Feb 8, 2013 |
10029924 |
|
|
16016631 |
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Current U.S.
Class: |
1/1 |
Current CPC
Class: |
C02F 2101/322 20130101;
C02F 2303/18 20130101; B01F 2215/0431 20130101; C02F 2303/185
20130101; B01D 19/0005 20130101; F04B 23/021 20130101; C02F 1/20
20130101; B01D 19/0042 20130101; B01D 19/00 20130101; B01F 3/04737
20130101; B01F 13/0049 20130101; C02F 2101/36 20130101; B01F
2215/0422 20130101; E03B 11/10 20130101; B01D 19/0047 20130101 |
International
Class: |
C02F 1/20 20060101
C02F001/20; B01F 3/04 20060101 B01F003/04; B01F 13/00 20060101
B01F013/00; B01D 19/00 20060101 B01D019/00 |
Claims
1. A method for treating water laden with trihalomethanes (THM) in
liquid state in an enclosed tank having a ceiling, floor, and side
walls extending between the ceiling and floor to contain the water
therein with the surface of the water spaced at least a first
distance below the ceiling of the tank to create an air gap region
between the ceiling and the surface of the water therebelow, said
method including the steps of: (a) providing a water circulation
system for creating a circulation pattern of the water laden with
THM in said tank (1) by continuously moving up a portion of the
water from the depths of the tank into an inlet of a draft tube and
up through said draft tube to a first location above the surface of
the remaining water and (2) by thereafter spraying the upwardly
moved portion of the water into the air gap region in a spray
pattern (i) outwardly above the surface of the remaining water in
the tank about a vertical axis toward the side walls of the tank
and (ii) with at least a portion of said spray pattern directed
slightly downwardly toward the surface of the remaining water
thereby continuously circulating the remaining water in the tank
radially outwardly of and about said vertical axis adjacent the
surface of the water in the tank toward said tank side walls,
downwardly along the tank side walls, and inwardly across the floor
toward the inlet to the draft tube with said portion thereof moved
upwardly through said draft tube to said first location above the
surface of the remaining water in the tank and sprayed outwardly
into said air gap region toward the surface of the remaining water
wherein the upwardly moved water portion laden with THM sprayed
into the air gap region is exposed to the air in said air gap
region and the THM in liquid state therein volatized by the air
exposure to a gaseous state in said air gap region and (b)
providing an air flow system for creating a continuous air flow
pattern directed above and across the surface of the remaining
water in the tank from ambient, atmospheric air outside of the tank
continuously through the tank from an inlet in the tank into the
air gap region above the surface of the remaining water in the tank
and back out of the air gap region above the surface of the
remaining water in the tank through an air outlet in the tank into
the ambient, atmospheric air by establishing a pressure
differential between the air inlet and the air outlet of the tank,
and further including the step that said provided air flow system
is further capable of directing at least a portion of said air flow
pattern toward and into the spray pattern of step (a)(2) of the
upwardly moved water portion above the surface of the remaining
water in the tank wherein the THM in liquid state upwardly moved
through the draft tube and volatized to gaseous state in the air
gap region above the surface of the remaining water in the tank
enters the air flow pattern in the tank above the surface of the
remaining water in the tank and exits the tank with the air flow
pattern through the air outlet of the tank.
2. The method of claim 1 wherein the provided water circulation
system is further capable of maintaining said first location of
said upwardly moved portion of the water at a predetermined
distance above the surface of said remaining water.
3. The method of claim 1 wherein the provided water circulation
system is further capable of varying the distance of the surface of
the remaining water in the tank below the ceiling of the tank and
maintaining said first location of said upwardly moved portion of
the water at a predetermined distance above the surface of said
remaining water.
4. The method of claim 1 wherein the provided water circulation
system further includes a flotation platform capable of supporting
the draft tube with said first location of the upwardly moved water
portion therethrough at a predetermined distance above the surface
of the remaining water in the tank.
5. The method of claim 1 wherein the provided water circulation
system is further capable of directing substantially all of the
upwardly moved water portion downwardly in step (a)(2).
6. The method of claim 1 wherein the provided water circulation
system is further capable of directing the spray pattern of step
(a)(2) downwardly about the vertical axis substantially in the
shape of an inverted cone.
7. The method of claim 1 wherein the provided water circulation
system is further capable of directing the spray pattern of step
(a)(2)(ii) downwardly substantially between 25 and 35 degrees to
the horizontal.
8. The method of claim 1 wherein the provided water circulation
system in step (a)(2) includes the further limitations of providing
a perforated sheet configured in an inverted, substantially conical
shape with the sides of the cone inclined upwardly and outwardly
relative to the vertical axis and the provided water circulation
system is capable of spraying the upwardly moved water portion of
step (a)((2)(ii) slightly downwardly toward the surface of the
remaining water through the perforations of the sheet.
9. The method of claim 8 wherein the provided water circulation
system is further capable of spraying the upwardly moved water
portion through said perforations slightly downwardly in step
(a)(2)(ii) between 25 and 35 degrees to the horizontal.
10. The method of claim 8 wherein the provided sheet is about 0.1
inches thick and has between 5,000 and 30,000 perforations
therethrough of about 0.01 inches in diameter.
11. The method of claim 1 wherein the upwardly moved water portion
of the provided water circulation system is capable of being drawn
into the inlet of the draft tube substantially radially across the
tank floor.
12. The method of claim 1 wherein the inlet to the draft tube of
the provided water circulation system is capable of being
positioned less than a foot from the tank floor.
13. The method of claim 1 wherein the volume of the upwardly moved
water portion per minute of the provided water circulation system
is capable of being less than one thousandth the volume of the
water in the tank.
14. The method of claim 1 wherein the pump of the provided water
circulation system is driven by a motor positioned in the draft
tube in the upwardly moved water portion wherein the upwardly moved
water portion of the provided water circulation system is capable
of cooling the motor and conversely heating the upwardly moved
water portion to aid in the rate and efficiency of the subsequent
volatilization of the THM.
15. The method of claim 1 wherein the provided air flow system is
capable of directing said portion of the air flow pattern
downwardly through a hose toward and into the spray pattern of step
(a)(2).
16. The method of claim 1 wherein the provided air flow system
further includes a hose capable of depending downwardly to adjacent
the surface of the remaining water in said tank and the provided
air circulation system is capable of directing said portion of the
air flow pattern through said hose downwardly toward said
surface.
17. The method of claim 16 wherein the provided air flow system is
further capable of depending said hose downwardly from the ceiling
of the tank.
18. The method of claim 16 wherein the provided air flow system is
further capable of depending said hose downwardly substantially
along and about said vertical axis of said spray pattern.
19. The method of claim 16 wherein the provided air flow system is
further capable of depending said hose downwardly to a second
location closer to said tank ceiling than said first location of
said drawn-up water portion of step (a)(1) of the provided water
circulation system.
20. The method of claim 1 wherein the provided air flow system is
further capable of establishing said pressure differential between
the air inlet of the tank and the air outlet of the tank by
pressuring the ambient air entering the air inlet to above
atmospheric.
21. The method of claim 1 wherein the provided air flow system is
capable of having the air flow of step (b) in cubic feet per minute
between the tank inlet and outlet to be between 15 and 30 times the
flow of the upwardly moved water portion of step (a)(1) of the
provided water circulation system in cubic feet per minute.
22. The method of claim 1 wherein the provided water circulation
system is further capable of maintaining said first location of
said upwardly moved portion of water at a predetermined, fixed
distance below the ceiling of the tank.
23. The method of claim 1 wherein the provided water circulation
system is further capable of varying the distance of the surface of
the remaining water in the tank and maintaining said first location
of said upwardly moved portion of water at a predetermined, fixed
distance below the ceiling of the tank.
24. The method of claim 1 wherein the provided water circulation
system further includes a perforated hose substantially
concentrically surrounding said draft tube substantially at said
first location and the provided air flow system is capable of
directing said air portion of step (b) into the space between the
draft tube and surrounding, perforated hose.
Description
RELATED APPLICATIONS
[0001] This application is a division of U.S. patent application
Ser. No. 13/763,379 filed Feb. 8, 2013, which is incorporated
herein by reference and the benefit of which is hereby claimed.
BACKGROUND OF THE INVENTION
1. Field of the Invention
[0002] This invention relates to the field of systems for treating
potable water in municipal and similar tanks to reduce and remove
undesirable disinfectant byproducts from the water.
2. Discussion of the Background
[0003] Potable bodies of water and in particular municipal and
other water sources intended for drinking are commonly treated with
disinfectants such as chlorine and chloramines. These disinfectants
very efficiently and effectively eliminate harmful agents in the
water making the water potable and suitable for drinking. However,
such disinfectants can and usually do create undesirable
disinfectant byproducts such as chloroform, bromodichloromethane,
dibromochloromethane, and bromoform which are all forms of
trihalomethanes (THM's). In very small amounts (e.g., very low
parts per billion), these THM's are not believed to be a serious
threat to health but reduction of them in potable water reservoirs
such as municipal water tanks is always desirable and is
increasingly being mandated by law.
[0004] With this and other problems in mind, the present invention
was developed. In it, a water circulation system and an air flow
system are each created within an enclosed tank to interact and
intersect with each other to greatly enhance the volatizing of
undesirable disinfectant byproducts such as THM's in liquid state
in the water to gaseous state to then be vented out of the
tank.
SUMMARY OF THE INVENTION
[0005] This invention involves a method and apparatus for treating
potable water in municipal and similar tanks to reduce and remove
undesirable disinfectant byproducts such as trihalomethanes from
the water. The method and apparatus include providing a water
circulation system to create a circulation pattern in the tank
water and an air flow system for creating an air flow pattern in
the air gap or headspace region of the enclosed tank above the
water surface.
[0006] In operation, a portion of the tank water is drawn-up a
draft tube from essentially at the tank floor to a first location
above the water surface. In the preferred embodiment, the drawn-up
water portion is then sprayed through a nozzle at the first
location outwardly about a vertical axis and slightly downwardly
toward the surface of the remaining water in the tank. In doing so,
a driving pattern is established in the remaining water in the tank
that initially moves radially outwardly from the nozzle toward the
tank side walls, downwardly along the side walls, radially inwardly
across the tank floor toward the inlet of the draft tube, and up
the draft tube to the nozzle. This driving pattern in turn induces
a secondary circulation pattern within it to very effectively and
thoroughly mix or blend all of the water in the entire tank.
[0007] The air flow system in turn creates a high volume of air
passing into and out of the tank in the air gap or headspace region
above the water surface. The air flow system of the preferred
embodiment drives ambient air through a tank inlet downwardly
toward the water surface with at least a portion of the air flow
pattern directed toward and into the spray pattern of the nozzle.
The undesirable trihalomethanes in liquid state in the drawn-up
water portion are then exposed in the spray pattern to air and
volatize to gaseous state where they enter the air flow pattern and
exit the tank through the tank outlet into ambient air. Other
portions of the air in the flow pattern passing across the surface
of the tank water also aid in volatizing the undesirable
trihalomethanes.
BRIEF DESCRIPTION OF THE DRAWINGS
[0008] FIG. 1 is a cross-sectional view of a municipal tank with
the preferred embodiment of the present invention in it.
[0009] FIGS. 2 and 3 illustrate the outer, driving and inner,
induced circulation patterns set up in the tank by the water
circulation system of the present invention.
[0010] FIG. 4 is a top plan view taken along line 4-4 of FIG. 2
further illustrating the driving water pattern set up adjacent the
surface of the tank water.
[0011] FIG. 5a is an enlarged, partial cross-sectional view of the
nozzle at the top of the draft tube and the spray pattern it
creates to produce the driven water pattern in the surface of the
tank water.
[0012] FIG. 5b is a further enlarged view of the perforations in
the nozzle.
[0013] FIG. 6 is a cross-sectional view of the water circulation
system and the air flow circulation system of the present invention
in operation.
[0014] FIG. 7 is an enlarged view of the interaction of the water
circulation system and air flow system of the present
invention.
[0015] FIG. 8 illustrates the preferred embodiment in operation to
volatize the undesirable byproducts such as trihalomethanes in
liquid state in the water to a gaseous state and to remove them
from the tank.
[0016] FIG. 9 is a view similar to FIG. 6 with the depending air
hose and nozzle of the draft tube slightly misaligned but still
operating in the desired manner of FIG. 6 to volatize and remove
undesirable byproducts such as trihalomethanes from the tank
water.
[0017] FIG. 10 illustrates a second embodiment of the present
invention.
[0018] FIG. 11 is an enlarged view of the nozzle of the second
embodiment.
[0019] FIGS. 12a and 12b are further enlarged views of the nozzle
of the second embodiment.
DETAILED DESCRIPTION OF THE INVENTION
[0020] The method and apparatus of the present invention are
primarily designed for use in a municipal or similar, potable water
tanks such as 2 in FIG. 1 to aid in removing undesirable byproducts
of the disinfectant process or processes from the water 4. Such
undesirable byproducts as discussed above include trihalomethanes
(THM) and similar byproducts of disinfecting processes,
particularly those processes using chlorine and chloramines which
routinely result in undesirable concentrations of THM in liquid
state remaining in the processed water. As shown in FIG. 1,
municipal water tanks such as 2 commonly include a ceiling 6 and
floor 8 with side walls 10 extending therebetween to contain the
water 4 in the tank 2. The water 4 can enter and exit the enclosed
tank 2 in any number of manners including via the illustrated inlet
and outlet pipes 12,12' of FIG. 1. The entering flow through inlet
pipe 12 is typically controlled as for example by an upstream valve
or pump at 14 that can be selectively operated in response to high
and low water level sensors such as 16,16' in the tank 2. The
surface 18 of the water 4 is then spaced at least a first distance
(e.g., 4 to 6 feet) below the ceiling 6 by the high level sensor 16
to create an air gap or headspace region 20 above the surface 18 of
the water 4.
[0021] As schematically shown in FIG. 1, the present invention
includes a water circulation system 1 having a flotation platform 3
with a draft tube 5 depending downwardly therefrom to the water
inlet 7 of the draft tube 5 adjacent the floor 8 of the tank 2. In
operation as best seen in FIGS. 2-3, the pump 9 positioned within
the draft tube 5 in FIG. 2 draws up water 4' from substantially at
the tank floor 8 (e.g., within a foot or so and preferably within
six or fewer inches) into the inlet 7 of the draft tube 5 and up
through the draft tube 5 to a spray nozzle 11. The spray nozzle 11
as shown in FIGS. 2-3 is supported by the flotation platform 3
above the water surface 18'' of the remaining water 4'' in the tank
2. The drawn-up water portion 4' through the draft tube 5 is then
sprayed through the nozzle 11 at 13 in FIG. 2 outwardly and
slightly downwardly toward the water surface 18''. In doing so, a
driving pattern or circulation 15 (see FIG. 3) is established in
the remaining water 4'' in the tank 2. This driving pattern 15 as
illustrated in FIGS. 3 and 4 initially moves substantially radially
outwardly from the nozzle 11 substantially 360 degrees about the
vertical axis 17 at the water surface 18'' (FIG. 4). The driving
pattern 15 then continues outwardly toward the side walls 10 of the
tank 2 (FIG. 3), downwardly along the side walls 10, radially
inwardly across the tank floor 8 toward the inlet 7 of the draft
tube 5, and up the draft tube 5. This driving pattern or
circulation 15 in turn induces a secondary circulation pattern at
19 in FIG. 3 within the outer, driving pattern 15 to very
effectively and thoroughly mix or blend all of the water in the
entire tank 2. The inner or secondary circulation pattern 19 as
shown in FIG. 3 passes up adjacent the outside of the draft tube 5
toward the water surface 18'' and outwardly immediately beneath the
upper flow 15 of the driving pattern to pass outwardly and
downwardly within the driving pattern 15 and again up adjacent the
draft tube 5.
[0022] The spray nozzle 11 of FIG. 5a is preferably a very thin
(e.g., 0.1 inch) sheet 21 of stainless steel or similar material
that has been pierced to create a large number (e.g., 5,000-30,000)
of holes or perforations 23 on the order of 0.01 inches in diameter
(FIG. 5b). The sheet 21 is then formed into an inverted,
substantially conical or frustoconical shape about the vertical
axis 17 (FIG. 5a). The apex area of the inverted cone is preferably
about a foot above the water surface 18'' of FIG. 3 and the height
of the inverted cone itself from the apex to its base is preferably
on the order of about 18 inches. The sides of the cone extend
upwardly and outwardly of the vertical axis 17 on the order of 25
to 35 degrees. The pierced holes or perforations 23 are preferably
directed outwardly about the vertical axis 17 and then slightly
downwardly (e.g., 25 to 35 degrees and preferably about 30 degrees)
from the horizontal 25 in FIG. 5a into the air gap region 20 (FIGS.
2-3) above the water surface 18''. In doing so, the pierced holes
23 preferably create very fine streamlets or streamlines of water
that will not only drive the circulating pattern 15 of FIG. 3 in
the remaining water 4'' but also allow space in between the
streamlines for air as the streamlines in part (e.g., 50%)
transition to propelled droplets and mist. The upper or higher
streamlines 13 adjacent the inverted base of the cone of the nozzle
11 in FIGS. 2-4 extend out to or slightly beyond the floats 3' of
the flotation platform 3 (FIG. 4) or roughly on the order of 3-6
feet outwardly from the vertical axis 17 (FIGS. 2-3) before
striking the water surface 18''. This in turn has been found to
provide sufficient hang time for all of the streamlines 13 to be
exposed to the air in the spray pattern to effectively treat or
volatize the THM laden water. Empirically, in a tank 35 feet high
and 100 feet in diameter holding about 2,000,000 gallons of water,
it has been found that a pressure within the nozzle 11 of around
15-25 psi works very well in this regard. It is noted that although
the water portion 4' is preferably drawn-up or upwardly move at a
fairly high rate (e.g., 500 gallons per minute), the relative
volume of this drawn-up water portion 4' per minute compared to the
total volume of the tank (e.g., 2,000,000 gallons in a 35 foot high
tank with a 100 foot diameter) is relatively small or less per
minute than one thousandth of the total tank volume.
[0023] The present invention also includes an air flow system (FIG.
6) that creates an air flow pattern in the air gap region 20 above
the water surface 18''. This air flow system and air flow pattern
are in addition to the above-described water circulation system 1
of FIG. 3 that creates the water flow patterns 15 and 19 in the
water in the tank 2. The water and air flow systems interact and
preferably actually intersect in the area of the spray pattern 13
from the nozzle 11 above the water surface 18'' as in FIGS. 6-7.
More specifically, the enclosed tank 2 of FIG. 6 is provided with
an air fan or blower at 32. The blower 32 as shown draws in
ambient, atmospheric air at 34, pressurizes it, and drives it down
the depending hose 36 toward the water surface 18'' and preferably
directly into the spray pattern 13 from the nozzle 11. The end of
the hose 36 is preferably adjacent the water surface 18'' but still
at a location closer to the ceiling 6 than the nozzle 11. The tank
2 is vented at 40 and the illustrated air flow pattern of FIG. 6 is
then created from ambient, atmospheric air at 34 down the hose 36
into the air gap region 20 of the tank 2 and back out of the air
gap region 20 through the air outlet 40 into the ambient,
atmospheric air. Depending upon the size of the tank 2 and its air
gap region 20, the air flow in cubic feet per minute is preferably
on the order of 15-30 times (e.g., 20:1) the flow of the drawn-up
portion of water 4' in cubic feet per minute. As for example and in
a tank 35 feet high and 100 feet in diameter with an air gap region
20 extending 4-6 feet down from the tank ceiling 6 and a drawn up
water portion 4' of 500 gallons per minute (roughly 70 cubic feet
per minute), a desirable volume of air passing through the tank 2
would be on the order of 1400 cubic feet per minute. This would
deliver an air volume enough to displace an air gap region 20 on
the order of 6 feet high and 100 feet in diameter in our examples
in about 30 minutes.
[0024] Such a high volume of change-out air is desirable to keep
the air gap region 20 particularly near the nozzle spray pattern 13
and water surface 18'' from becoming saturated with gaseous THM
that might then condense and return to the water. Also, the
volatilization process of the liquid state THM to gaseous state
consumes heat from the air thereby reducing the air and water
temperatures. The reduced temperatures in turn reduce the
efficiency of the volatilization process wherein the preferred,
relatively high air change-out rate then desirably adds heat to the
air in the air gap region 20 to thereby increase the rate and
efficiency of the volatilization process. Similarly, it is noted
that the motor 9' for the pump 9 in FIGS. 2 and 7 is preferably
positioned within the flow of the drawn-up or upwardly moved water
portion 4' in the draft tube 5. In this manner and on the one hand,
the passing flow of 4' then cools the motor 9' and on the other
hand, the passing flow of 4' is conversely and advantageously
heated to aid in the subsequent volatilization process at the
nozzle 11. The driving, air pressure differential (e.g., 1/5- 1/10
psi) between the tank inlet and outlet could also be created by
reversing the flow through the blower 32 if desired but it is
preferably created as illustrated in FIG. 6. Regardless and as
mentioned above, the water and air flow patterns preferably
actually intersect in the area of the spray pattern 13 from the
nozzle 11 above the water surface 18'' as perhaps best seen in FIG.
7. It is noted that the force of the water spray pattern 13 itself
from the nozzle 11 into the air gap region 20 also aids in inducing
the overall air currents in the tank 2 and in drawing air into the
water spray pattern 13 itself and over the water surface 18''.
[0025] In this manner, the volatizing or conversion of undesirable
byproducts such as trihalomethanes (THM) from a liquid state in the
tank water to a gaseous state in the air gap region 20 is greatly
enhanced. That is and as perhaps best seen in FIG. 8, the THM in
liquid or aqueous state resulting from the disinfectant process or
processes discussed above is normally denser than water per se and
tends to settle and concentrate in the tank water closest to the
tank floor 8. This is the case whether the water is treated
upstream of the tank 2 or actually in the tank 2. In either event,
the water circulation system 1 of the present invention as
explained above will then continuously draw up water laden with THM
in liquid state from the depths of the tank 2 substantially at the
tank floor 8 into the inlet 7 of the draft tube 5 and up through
the draft tube 5 to a first location at the nozzle 11. This first
location at the nozzle 11 as illustrated in FIGS. 2 and 3 is above
the water surface 18'' of the remaining water 4'' in the tank 2 and
the drawn-up water portion 4' (FIG. 3) through the draft tube 5 is
thereafter sprayed into the air gap region 20 above the water
surface 18'' in a spray pattern 13. The spray pattern 13 as
discussed above is substantially radially outwardly above the water
surface 18'' substantially 360 degrees about the vertical axis 17
of FIGS. 2-4 toward the side walls of the tank 2. The spray pattern
13 is also directly slightly downwardly (e.g., 30 degrees from the
horizontal 25 as in FIG. 5a) toward the water surface 18'' to
create the driving flow pattern 15 of FIG. 3 in the tank water. In
this embodiment, substantially all of the spray pattern is
preferably directed downwardly to create as strong a driving
pattern 15 as possible.
[0026] The discharge of pressurized, ambient air exiting the hose
36 in FIG. 8 is then preferably directed downwardly as also
discussed above along the vertical axis 17 into the spray pattern
13 from the nozzle 11 to greatly enhance the contact and volatizing
of the THM in liquid state to THM in gaseous state. The THM in
gaseous state then enters the rest of the air flow pattern as in
FIG. 8 and exits with the air flow out the vent 40 into the ambient
air. Although the discharged air from the hose 36 is preferably
directly downwardly along and about the vertical axis 17 directly
and uniformly into the spray pattern 13 from the nozzle 11 as
illustrated in FIG. 8, enhanced contact and volatizing of the THM
in liquid state with the air in the air gap region 20 will also
occur even if the hose 36 and nozzle 11 are slightly misaligned as
in FIG. 9. Such misalignment can occur as a result of the initial
setup or due to the flotation platform and nozzle 11 moving
laterally as the water level rises or falls in the tank 2.
Regardless, the enhanced contact and volatizing will occur to at
least a certain extent with even just at least a portion of the
discharged air from the hose 36 directed toward and into the nozzle
spray pattern 13 as in FIG. 9. In both the aligned and misalignment
positions, the discharged air exits the hose 36 relatively close to
the water surface 18'' and will also move outwardly adjacent the
surface 18'' toward the tank walls 10 to help volatize and entrain
gaseous THM in the overall air flow pattern.
[0027] It is noted that the water circulation system 1 of the
present invention is a paramount feature. This is the case
particularly as the system 1 draws up water essentially at the tank
floor 8 (e.g., within a foot or so and preferably within six or
fewer inches) as in FIGS. 2-3 and establishes the primary or
driving circulation pattern 15 (FIG. 3) and the induced secondary
or inner circulation pattern 19 that effectively and thoroughly mix
or blend the water in the entire tank 2. In doing so, the water
circulation system 1 results in virtually all of the tank water in
a relatively short period (e.g., 1-2 days in the 2,000,000 gallon
tank of our examples) being passed through and treated in the
relatively small area (e.g., 6-12 feet wide and 30 inches high) of
the substantially conical spray pattern 13 from the nozzle 11. This
is in contrast to other systems that do not have such a localized
treatment area and need to have treatment zones virtually
throughout the entire tank to ensure proper treatment. It is also
in contrast to many prior art systems in which the water being
sprayed and treated is only from a very limited area in the tank
often just in the immediate vicinity of the pump. The same
relatively small amount of water adjacent the pump is then just
continually recycled leaving the rest of the water untreated.
Further, if the drawn up water is not essentially from right off
the tank floor (e.g., twelve inches or fewer), the denser THM may
simply pass into and out of the tank along the tank floor 8 in the
configuration of FIG. 3 without being treated at all. In
comparison, the water circulation system 1 of the present invention
as discussed above not only draws up water essentially at and
across the entire tank floor 8 but also establishes a complete
circulation throughout the tank with few if any dead spots where
THM might undesirably concentrate. Monitoring samples for THM
concentrations can then be taken essentially anywhere in the tank 2
with the confidence that the readings will accurately reflect the
THM concentrations everywhere in the tank 2. The fresh air flow
system is equally important to the present invention as it
virtually eliminates the undesirable situation that volatized THM
will saturate the air in the air gap region 20 with the gaseous THM
then undesirably condensing and returning to the water.
[0028] It is also noted that the flotation platform 3 of FIGS. 2-4
with the draft tube 5 depending therefrom and the nozzle 11
supported thereon is preferred. This is the case because the pump 9
of FIG. 7 is then always at a predetermined, fixed depth or
distance below the water surface 18'' as the tank water level rises
or falls. Conversely, the nozzle 11 is always at a predetermined,
fixed distance or location above the water surface 18''. In this
manner, the operating parameters of this embodiment including the
power requirements of the motor 9' for the pump 9 can best be
designed and optimized for highest efficiency and safety to the
various parts of the water circulation system and the air flow
system of the present invention. Although the embodiment of FIG.
1-9 is preferred, the driving pump (see 9'' in FIGS. 10-11) could
also be positioned on the tank floor 8 if desired and the nozzle
(11' in FIGS. 10-11) suspended at a predetermined, fixed location
from the tank ceiling 6 as the water surface 18 (FIG. 10) may vary
by rising or falling. The motor 9''' for the pump 9'' in FIG. 11 as
is the case with motor 9' for the pump 9 in FIG. 2 of the first
embodiment can be powered by an electrical cord 31 (FIG. 10)
dropping down through or adjacent the air hose 36', which power
cord 31 is only shown in FIG. 10 for clarity. Additionally, the
motor 9''' in the embodiment of FIG. 10 like the motor 9' in the
first embodiment is preferably positioned within the flow of the
water portion 4'. As discussed above and on the one hand, the
passing flow of 4' then cools the motor 9''' and on the other hand,
the passing flow of 4' is conversely and advantageously heated to
aid in the subsequent volatilization process at the nozzle 11'.
[0029] The modified nozzle 11' as shown in FIGS. 12a and 12b
includes the upcoming water tube 5' that is concentrically
surrounded by the lower extension 36'' of the depending air hose
36'. A plurality of radially spaced nozzles 11'' are then provided
at upper and lower levels on the water tube 5' and the surrounding
extension 36'' provided with perforated air holes 23' above and
below the nozzles 11'' as shown in FIGS. 12a-12b. The spray pattern
13' of FIG. 11 from the nozzle 11' differs from nozzle 11 of the
preferred embodiment of FIGS. 1-9 but still has a component
directed radially outwardly substantially 360 degrees about the
vertical axis 17' and slightly downwardly toward the water surface
18'' to create a water driving pattern like 15 in FIG. 3.
Similarly, the pressurized air discharged through the perforated
air holes 23' creates an air flow pattern in the air gap region 20
in part like the air flow pattern illustrated in FIG. 6. To a
certain extent, the choice between the embodiments of FIGS. 1-9 and
10-12b depends upon the size of the access opening to the tank with
the first embodiment normally requiring a larger one (e.g., 18
inches or more).
[0030] The above disclosure sets forth a number of embodiments of
the present invention described in detail with respect to the
accompanying drawings. Those skilled in this art will appreciate
that various changes, modifications, other structural arrangements,
and other embodiments could be practiced under the teachings of the
present invention without departing from the scope of this
invention as set forth in the following claims. In particular, it
is noted that the undesirable byproducts to be treated by the
present invention have been primarily described as being
trihalomethanes (THM) resulting from disinfecting processes that
use chlorine and chloramines. Such THM exist in liquid state in the
processed water and have a relatively high vapor pressure while
having a relatively low aqueous solubility. Consequently, THM in
liquid state in water easily and quickly volatizes to a gaseous
state when exposed to air. However, the method and apparatus of the
present invention are meant to equally encompass treating similar
byproducts from other disinfecting processes in which the processed
water has undesirable byproducts with similar properties to THM
including a relatively high vapor pressure so it easily and quickly
volatizes into air. It is also noted that the word substantially is
utilized herein to represent the inherent degree of uncertainty
that may be attributed to any quantitative comparison, value,
measurement or other representation. This term is also utilized
herein to represent the degree by which a quantitative
representation may vary from a stated reference without resulting
in a change in the basic function of the subject matter
involved.
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