CA1088228A - Aeration method and system - Google Patents
Aeration method and systemInfo
- Publication number
- CA1088228A CA1088228A CA292,651A CA292651A CA1088228A CA 1088228 A CA1088228 A CA 1088228A CA 292651 A CA292651 A CA 292651A CA 1088228 A CA1088228 A CA 1088228A
- Authority
- CA
- Canada
- Prior art keywords
- chamber
- extending
- gas
- section
- water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 238000000034 method Methods 0.000 title abstract description 4
- 238000005273 aeration Methods 0.000 title description 5
- 238000002156 mixing Methods 0.000 claims abstract description 55
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 37
- 239000002351 wastewater Substances 0.000 claims abstract description 34
- 238000005086 pumping Methods 0.000 claims description 8
- 239000007788 liquid Substances 0.000 claims description 5
- 238000007667 floating Methods 0.000 claims description 2
- 238000007654 immersion Methods 0.000 claims 1
- 238000007664 blowing Methods 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 12
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 8
- 239000001301 oxygen Substances 0.000 description 8
- 229910052760 oxygen Inorganic materials 0.000 description 8
- 241000894006 Bacteria Species 0.000 description 3
- 239000004033 plastic Substances 0.000 description 3
- 238000005276 aerator Methods 0.000 description 2
- 238000011010 flushing procedure Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000011152 fibreglass Substances 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Abstract
ABSTRACT OF THE DISCLOSURE
An improved method and system for mixing gas with waste water in which the water is pumped through a plurality of mixing chambers into which the gas is injected at a step region to form parallel streams of gas and water.
An extending chamber contains the parallel streams as the interface between them becomes unstable, breaks down creating vortices and produces tiny bubbles which mix with the water.
The extending chamber is tapered inwardly to permit opera-tion at higher air flow rates without blowing the bubble forming vortices out of the chamber. Helical vanes are preferably provided in the bores which inject the air into the extending chamber to create better wave generating conditions to extend the range to greater air flow rates.
An improved method and system for mixing gas with waste water in which the water is pumped through a plurality of mixing chambers into which the gas is injected at a step region to form parallel streams of gas and water.
An extending chamber contains the parallel streams as the interface between them becomes unstable, breaks down creating vortices and produces tiny bubbles which mix with the water.
The extending chamber is tapered inwardly to permit opera-tion at higher air flow rates without blowing the bubble forming vortices out of the chamber. Helical vanes are preferably provided in the bores which inject the air into the extending chamber to create better wave generating conditions to extend the range to greater air flow rates.
Description
BRIE~' DESCRIPTION OF THE INVENTION
AND SUMMARY OF THE INVENTION:
~ he invention relates to an improved method, and submerged system for efficiently mixing gas with wate water.
Industrial waste, sawage and the like are com-monly purified by pumping the liquid into a large pond, tank or basin where a bacteria population consumes the inorganic and organic material. Because the dissolved oxygen in the waste water is usually insufficient to support the required population of bacteria, the water must be aerated. This can be done with a surface aerating machine which has beaters extending into the waste water from above the water surface to agitate the water and incorporate air. Alternatively, air can be diffused through the bottom of the basin, e.g., through a porous medium. Surface aerators are not efficient and ~ause certain mechanical problems.
the energy loss of diffusing air is also great and a diffused system is not suitable for insta}lation in an existing pond.
~ he waste water can also be aerated by pumping through submerged tubes with Venturi openings through which air is drawn or pumped into the tubes to create turbulent mixing.
The present invention relates to an improved method and system for mixing a gas such as oxygen or air with waste ~-water. The system includes a plurality of mixing chambers which are disposed below the surface of the waste water and through which the water is pumped from an inlet to an outlet.
A suitable gas, such as oxygen or air containing oxygen, is injected into each of the mixing chambers at a step region to form parallel streams of air and water in an extending chamber. As the two streams move down the extending chamber, the interface between the two streams becomes unstable and waves form which attach to the sides of the chamber. This causes large frictional stresses, creating tiny bubbles which mix with the water. Since the water and air essentially flow in the same direction, no energy is wasted in turbulence and the system is energy efficient. Systems of this type are described and claimed in our co-pending Canadian application Serial No. 292,705 filed December 8, 1977.
According to an improved aspect of this system, the mixing chamber is preferably tapered in the downstream direction, first gradually and then radically, to ensure that the vortices created by the mixing do not extend out of the chamber which would reduce the efficienoy of `-the mixing. Further, helical vanes are preferably provided in the injection bores for the gas to create greater wave generating conditions which extend the - -~
operating range of the device to greater air flow rates.
10~822~
This system can be quickly and easily in-stalled in any existinq aeration pond without the need for the system to be shut down for an extended period and without the need for the pond to be drained, a S project which is difficult or impossible in most in-stances. The system can, in fact, be installed and operating within a few minutes. In comparison with diffused air type devices and surface aeration systems, the energy required to incorporate a given amount of oxygen into the water is much less. Because little energy is wasted in turbulent mixing, the present inven-tion is more energy efficient than Venturi, jet or impingement t~e svstems which depend on turbulent mixing. Further, the bubbles which are produced are tiny, thus creating a good environment for effective use of the oxygen by the bacteria within the pond or basin. Many of the other disadvantages of surface aera-tors and diffusion type devices are also avoided.
Other objects and purposes of the invention will be clear from the following detailed description of the drawings.
BRIEF DESCRIPTION OF THE DRAWINGS:
-~IGURE 1 shows a schematic side view of the system of the present invention in use;
FIGURE 2 shows a planar view of the system of FIGURE l;
FIGURE 3 shows a sectional view of a mixing chamber of the present invention without helical vanes;
FIGURE 4 shows a front view of a mixing chamber with helical vanes;
~~; FIGURE 5 shows a partial sectional view of ;~ - 5 -'. ' ' ' .
10~82Z8 the mixing chamber of FIGURE 4;
FIGURE 6 shows a schematic view of another embodiment;
FIGURES 7 and 8 show a further embodiment.
DETAILED DESCRIPTION OF THE DRAWINGS: .
Reference is now made to FIGURES 1 and 2 which schematically illustrate one embodiment of the present invention. In the embodiment of FIGURES
1 and 2, a plurality of circumferentially disposed mix-ing chambers 20, each preferably identical to the other, are circularly disposed around a dome manifold 22 whioh includes an upper section 24 into which water is pumped and a lower section 26 connected to a source of air or oxygen at a ~uita`ble pressure. Each of the mixing chambers is of the type shown in detail in FIGURES 3-5 and discussed in detail below.
A plurality of conduits 30, each formed of a metal segment 32 and a plastic segment 34, connect sectio~ 24 to each mixing chamber 20 so that water is continuously pumped through each chamber 20. A similar series of conduits 40, each formed of a metal portion 42 and a plastic portion 44, connect section 26 to each of the mixing chambers 20. Each of the mixing chambers 20 forms parallel streams of air and gas which interact within an extending passage in the mixing chamber to form tiny bubbles which efficiently mix with the pumped waste water as it passes between an inlet and outlet.
.. ~ .
...
Manifold 22 is suspended from a fibreglass floating work platform 50 by means of guide bars 52, 54, and two bars behind bars 52 and 54. Industrial air pip-ing conduit 60 is attached to guide bar 54 for supply-ing air to section 26. Cable 62 connects the manifold 22 to a frame 64 on platform 50 for lifting manifold 22 and holding manifold 22 in position for maintenance.
Conventional submerged pump 66 is mounted above manifold 22 and includes a self-cleaning strainer bas-ket 67 over the pump intake which keeps most debris from entering the pump. For many installations the basket can be omitted and the debris which collects in the pump back-flushed as described below. When a basket is used, the small particles which accumulate on the outside of basket 67 are removed by back-flushing.
Conduit 68 connects pump 66 to section 24.
Platform 50 is provided with suitable railings 70 of a height so that the unit can be lifted to a level for convenient work on the mixing chambers 20 and pump 66. An on-shore air pump 74 is schematically shown as connected to line 60 for pumping air, oxygen or other gas to section 26 for mixing with the pumped waste water.
When it is desired to clean the inevitable particles and debris which will accumulate on basket 67, within pump 66 and within mixing chamber 20, pump 66 can simply be turned off while the air pump 74 continues forcing air into mixing chambers 20. Surprisingly, inst~ad of moving out of the outlet of each chamber, the 1~88Z28 air will pump waste water back through the inlet opposite to the direction of flow during aeration, through conduits 34 and 32 into section 24 through conduit 68 and through pump 66 blowing off the debris which has accumulated on the outside of strainer basket 67. This aspect of the invention is claimed in our co-pending Canadian application 292,707 filed December 8, 1977. This occurs because the water pressure at the level of the strainer basket is lower than the water pressure at the level of the mixing chambers 20.
Alternatively, flushing can be accomplished by operating a valve 76 in a line 78 which connects to conduit 68. The dehris will now be blown into the air and since the pressure differential is greater, the force produced, by the air which works as an air hammer, will blow the debris -through the system and back-flush all of the material in a few minutes.
FIGURES 3-5 illustrate two embodiments of the unique mixing chamber 20 of the present invention. Waste water flows from the inlet through passage 100 into the extending chamber 102. At the entry of passage 100 into chamber 102, a step region 104 is provided which includes a plurality of bores. The bores inject gas at an angle between roughly 11 and 22-1/2. To keep the vortices within extending chamber 102 at high air pressures, a chamber 110 with helical vanes 106 in the bores as shown in FIGURES 4 and 5 creates greater wave generating conditions, as the water enters an extending chamber (not shown) similar to the chamber 102 shown in FIGURE 3.
.. , ~ .
1088Z'~
Thus, two parallel streams of gas and waste water are created as shown in FIGURE 3. As the streams move along the chamber 102, the friction between them causes waves to form and air thus trapped in the waves to disperse into tiny bubbles. Since the air and gas streams mo~e in the same direction, effective mixing is -achieved at minimum energy consumption. It is desirable that under most conditions the mixing take place within chamber 102 and for that reason the chamber is slightly tapered inwardly within the section 110 with the cross-section decreasing in the direction from inlet to outlet and more radically tapered inwardly within sec-tion 112 at a rate greater than for section 110. These tapers extend the maximum air flow rate with which the system will operate by several times without substantial loss of efficiency.
The helical guide vanes 106 provide a twisting motion to the air and thus create more waves which also help the interface break up more quickly by creating 2Q instability.
The mixing chambers can be made of any suitable materials such as stainless steel, aluminum or plastic.
FIGURE 6 shows another embodiment in which the submersible pump is replaced with a conventional waste water pump 200 mounted beside tank 202 and connected to manifold 204 by line 206. Pump 200 has an inlet 207. A
plurality of mixing chambers 208 are mounted about mani-fold 204. Air pump 210 is also mounted beside tank 202 _ g _ 10~8228 and is connected to manifold 204 by line 212. Valve 214 can be opened to back-flush waste water as described above while pump 200 is turned off and pump 210 con-tinues to force gas into the mixing chambers 208. The gas then pumps the waste water back through ' manifold 204 and line 212 where it leaves via valve 214. The waste water returns to the tank and the debris is caught in a strainer 216 if desired.
FIGURES 7 and 8 illustrate yet another embodiment of the invention which utilizes mixing chambers as described above. In the arrangement of FIGURES 7 and 8, water in a suitable tank 300 is pumped through a straight line pipe 302 by a pump 304. A plurality of mixing chambers 306 extend outwardly from pipe 302at separated locations as shown in FIGURE 7. Air is supplied to a second pipe 308 which extends above and parallel to pipe 302. Alternatively, one pipe can be within the other.
Pipe 308 is connected to the individual mixing chambers for injecting air into those chambers. Pi~es 302 and 308 preferably extend along the center of the tank 300 parallel to the edges so as to cause a favorable pattern of water flow from one side to the other using a minimum amount of energy to create maximum flow and aeration. The system is flushed by opening valve 310 while pump 304 is turned off and air continued to be supplied to chambers 306.
~, ,. ..... . . . .
.- : . , .
Many changes and modifications in the above described embodiments of the invention can, of course, be carried out without departing from the scope of the invention. The system can be used with non-S aqueous li~uids and gas other than air, such as pureoxygen, can be added. Accordingly, that scope is in-tended to be limited only by the scope of the appended claims.
AND SUMMARY OF THE INVENTION:
~ he invention relates to an improved method, and submerged system for efficiently mixing gas with wate water.
Industrial waste, sawage and the like are com-monly purified by pumping the liquid into a large pond, tank or basin where a bacteria population consumes the inorganic and organic material. Because the dissolved oxygen in the waste water is usually insufficient to support the required population of bacteria, the water must be aerated. This can be done with a surface aerating machine which has beaters extending into the waste water from above the water surface to agitate the water and incorporate air. Alternatively, air can be diffused through the bottom of the basin, e.g., through a porous medium. Surface aerators are not efficient and ~ause certain mechanical problems.
the energy loss of diffusing air is also great and a diffused system is not suitable for insta}lation in an existing pond.
~ he waste water can also be aerated by pumping through submerged tubes with Venturi openings through which air is drawn or pumped into the tubes to create turbulent mixing.
The present invention relates to an improved method and system for mixing a gas such as oxygen or air with waste ~-water. The system includes a plurality of mixing chambers which are disposed below the surface of the waste water and through which the water is pumped from an inlet to an outlet.
A suitable gas, such as oxygen or air containing oxygen, is injected into each of the mixing chambers at a step region to form parallel streams of air and water in an extending chamber. As the two streams move down the extending chamber, the interface between the two streams becomes unstable and waves form which attach to the sides of the chamber. This causes large frictional stresses, creating tiny bubbles which mix with the water. Since the water and air essentially flow in the same direction, no energy is wasted in turbulence and the system is energy efficient. Systems of this type are described and claimed in our co-pending Canadian application Serial No. 292,705 filed December 8, 1977.
According to an improved aspect of this system, the mixing chamber is preferably tapered in the downstream direction, first gradually and then radically, to ensure that the vortices created by the mixing do not extend out of the chamber which would reduce the efficienoy of `-the mixing. Further, helical vanes are preferably provided in the injection bores for the gas to create greater wave generating conditions which extend the - -~
operating range of the device to greater air flow rates.
10~822~
This system can be quickly and easily in-stalled in any existinq aeration pond without the need for the system to be shut down for an extended period and without the need for the pond to be drained, a S project which is difficult or impossible in most in-stances. The system can, in fact, be installed and operating within a few minutes. In comparison with diffused air type devices and surface aeration systems, the energy required to incorporate a given amount of oxygen into the water is much less. Because little energy is wasted in turbulent mixing, the present inven-tion is more energy efficient than Venturi, jet or impingement t~e svstems which depend on turbulent mixing. Further, the bubbles which are produced are tiny, thus creating a good environment for effective use of the oxygen by the bacteria within the pond or basin. Many of the other disadvantages of surface aera-tors and diffusion type devices are also avoided.
Other objects and purposes of the invention will be clear from the following detailed description of the drawings.
BRIEF DESCRIPTION OF THE DRAWINGS:
-~IGURE 1 shows a schematic side view of the system of the present invention in use;
FIGURE 2 shows a planar view of the system of FIGURE l;
FIGURE 3 shows a sectional view of a mixing chamber of the present invention without helical vanes;
FIGURE 4 shows a front view of a mixing chamber with helical vanes;
~~; FIGURE 5 shows a partial sectional view of ;~ - 5 -'. ' ' ' .
10~82Z8 the mixing chamber of FIGURE 4;
FIGURE 6 shows a schematic view of another embodiment;
FIGURES 7 and 8 show a further embodiment.
DETAILED DESCRIPTION OF THE DRAWINGS: .
Reference is now made to FIGURES 1 and 2 which schematically illustrate one embodiment of the present invention. In the embodiment of FIGURES
1 and 2, a plurality of circumferentially disposed mix-ing chambers 20, each preferably identical to the other, are circularly disposed around a dome manifold 22 whioh includes an upper section 24 into which water is pumped and a lower section 26 connected to a source of air or oxygen at a ~uita`ble pressure. Each of the mixing chambers is of the type shown in detail in FIGURES 3-5 and discussed in detail below.
A plurality of conduits 30, each formed of a metal segment 32 and a plastic segment 34, connect sectio~ 24 to each mixing chamber 20 so that water is continuously pumped through each chamber 20. A similar series of conduits 40, each formed of a metal portion 42 and a plastic portion 44, connect section 26 to each of the mixing chambers 20. Each of the mixing chambers 20 forms parallel streams of air and gas which interact within an extending passage in the mixing chamber to form tiny bubbles which efficiently mix with the pumped waste water as it passes between an inlet and outlet.
.. ~ .
...
Manifold 22 is suspended from a fibreglass floating work platform 50 by means of guide bars 52, 54, and two bars behind bars 52 and 54. Industrial air pip-ing conduit 60 is attached to guide bar 54 for supply-ing air to section 26. Cable 62 connects the manifold 22 to a frame 64 on platform 50 for lifting manifold 22 and holding manifold 22 in position for maintenance.
Conventional submerged pump 66 is mounted above manifold 22 and includes a self-cleaning strainer bas-ket 67 over the pump intake which keeps most debris from entering the pump. For many installations the basket can be omitted and the debris which collects in the pump back-flushed as described below. When a basket is used, the small particles which accumulate on the outside of basket 67 are removed by back-flushing.
Conduit 68 connects pump 66 to section 24.
Platform 50 is provided with suitable railings 70 of a height so that the unit can be lifted to a level for convenient work on the mixing chambers 20 and pump 66. An on-shore air pump 74 is schematically shown as connected to line 60 for pumping air, oxygen or other gas to section 26 for mixing with the pumped waste water.
When it is desired to clean the inevitable particles and debris which will accumulate on basket 67, within pump 66 and within mixing chamber 20, pump 66 can simply be turned off while the air pump 74 continues forcing air into mixing chambers 20. Surprisingly, inst~ad of moving out of the outlet of each chamber, the 1~88Z28 air will pump waste water back through the inlet opposite to the direction of flow during aeration, through conduits 34 and 32 into section 24 through conduit 68 and through pump 66 blowing off the debris which has accumulated on the outside of strainer basket 67. This aspect of the invention is claimed in our co-pending Canadian application 292,707 filed December 8, 1977. This occurs because the water pressure at the level of the strainer basket is lower than the water pressure at the level of the mixing chambers 20.
Alternatively, flushing can be accomplished by operating a valve 76 in a line 78 which connects to conduit 68. The dehris will now be blown into the air and since the pressure differential is greater, the force produced, by the air which works as an air hammer, will blow the debris -through the system and back-flush all of the material in a few minutes.
FIGURES 3-5 illustrate two embodiments of the unique mixing chamber 20 of the present invention. Waste water flows from the inlet through passage 100 into the extending chamber 102. At the entry of passage 100 into chamber 102, a step region 104 is provided which includes a plurality of bores. The bores inject gas at an angle between roughly 11 and 22-1/2. To keep the vortices within extending chamber 102 at high air pressures, a chamber 110 with helical vanes 106 in the bores as shown in FIGURES 4 and 5 creates greater wave generating conditions, as the water enters an extending chamber (not shown) similar to the chamber 102 shown in FIGURE 3.
.. , ~ .
1088Z'~
Thus, two parallel streams of gas and waste water are created as shown in FIGURE 3. As the streams move along the chamber 102, the friction between them causes waves to form and air thus trapped in the waves to disperse into tiny bubbles. Since the air and gas streams mo~e in the same direction, effective mixing is -achieved at minimum energy consumption. It is desirable that under most conditions the mixing take place within chamber 102 and for that reason the chamber is slightly tapered inwardly within the section 110 with the cross-section decreasing in the direction from inlet to outlet and more radically tapered inwardly within sec-tion 112 at a rate greater than for section 110. These tapers extend the maximum air flow rate with which the system will operate by several times without substantial loss of efficiency.
The helical guide vanes 106 provide a twisting motion to the air and thus create more waves which also help the interface break up more quickly by creating 2Q instability.
The mixing chambers can be made of any suitable materials such as stainless steel, aluminum or plastic.
FIGURE 6 shows another embodiment in which the submersible pump is replaced with a conventional waste water pump 200 mounted beside tank 202 and connected to manifold 204 by line 206. Pump 200 has an inlet 207. A
plurality of mixing chambers 208 are mounted about mani-fold 204. Air pump 210 is also mounted beside tank 202 _ g _ 10~8228 and is connected to manifold 204 by line 212. Valve 214 can be opened to back-flush waste water as described above while pump 200 is turned off and pump 210 con-tinues to force gas into the mixing chambers 208. The gas then pumps the waste water back through ' manifold 204 and line 212 where it leaves via valve 214. The waste water returns to the tank and the debris is caught in a strainer 216 if desired.
FIGURES 7 and 8 illustrate yet another embodiment of the invention which utilizes mixing chambers as described above. In the arrangement of FIGURES 7 and 8, water in a suitable tank 300 is pumped through a straight line pipe 302 by a pump 304. A plurality of mixing chambers 306 extend outwardly from pipe 302at separated locations as shown in FIGURE 7. Air is supplied to a second pipe 308 which extends above and parallel to pipe 302. Alternatively, one pipe can be within the other.
Pipe 308 is connected to the individual mixing chambers for injecting air into those chambers. Pi~es 302 and 308 preferably extend along the center of the tank 300 parallel to the edges so as to cause a favorable pattern of water flow from one side to the other using a minimum amount of energy to create maximum flow and aeration. The system is flushed by opening valve 310 while pump 304 is turned off and air continued to be supplied to chambers 306.
~, ,. ..... . . . .
.- : . , .
Many changes and modifications in the above described embodiments of the invention can, of course, be carried out without departing from the scope of the invention. The system can be used with non-S aqueous li~uids and gas other than air, such as pureoxygen, can be added. Accordingly, that scope is in-tended to be limited only by the scope of the appended claims.
Claims (18)
1. A system for aerating waste water in a body of waste water comprising:
at least one mixing chamber for providing a waste water passage, including:
an extending chamber, a liquid passage for guiding waste water flow into said extending chamber, the cross-sectional area of the passage at the entry to said extending chamber being less than the cross-sectional area of said extending chamber at that entry so as to form a step region, and said extending chamber having at least a portion tapering inwardly in the direction away from said entry, and means defining at least one bore terminating in said step region for injecting gas into said extending chamber, to form parallel gas and water streams, said extending chamber extending downstream from said bore for confining flow of the parallel gas and water streams for a distance until the inter-face between said streams becomes unstable in said extending chamber and vortices are tripped to produce gas bubbles which are mixed with the water stream, means for pumping said waste water through said at least one mixing chamber, means for mounting said mixing chamber below the surface of said body of water, and means for injecting an aerating gas into waste water within said mixing chamber.
at least one mixing chamber for providing a waste water passage, including:
an extending chamber, a liquid passage for guiding waste water flow into said extending chamber, the cross-sectional area of the passage at the entry to said extending chamber being less than the cross-sectional area of said extending chamber at that entry so as to form a step region, and said extending chamber having at least a portion tapering inwardly in the direction away from said entry, and means defining at least one bore terminating in said step region for injecting gas into said extending chamber, to form parallel gas and water streams, said extending chamber extending downstream from said bore for confining flow of the parallel gas and water streams for a distance until the inter-face between said streams becomes unstable in said extending chamber and vortices are tripped to produce gas bubbles which are mixed with the water stream, means for pumping said waste water through said at least one mixing chamber, means for mounting said mixing chamber below the surface of said body of water, and means for injecting an aerating gas into waste water within said mixing chamber.
2. A system as in Claim 1, wherein said extending chamber has a first inwardly tapering section extending from said connection and a second section extending from said first section and tapering at a rate greater than the rate of taper of said first section.
3. A system as in Claim 1, including at least one helical vane disposed in each said bore for keeping the mixing within the extending chamber.
4. A system as in Claim 1, wherein said pumping means includes a water pump, and a first straight line pipe in said body having a plurality of said chambers extending outwardly therefrom and said injecting means includes a second straight line pipe in said body extending parallel to said first pipe and connected to said bores for supplying said gas thereto.
5. A system as in Claim 4, wherein said containing means is a tank and said pipes extend in the center of said tank.
6. A system as in Claim 1, wherein said injecting means includes a pump outside said body and means for connecting said pump to bores of said mixing chambers.
7. A system as in Claim 1, wherein said pumping means includes a pump, further including a manifold separated into a first section connected to said pump and to said inlets and a second section connected to said bores and to said gas injecting means, said chambers extending radially outward from said first section.
8. A system as in Claim 7, including means for mounting said pump above said manifold in said body, said pump having an inlet in said body.
9. A system as in Claim 8, including a strainer basket over the inlet of said pump.
10. A system as in Claim 8, wherein said connecting means includes a conduit between said pump and manifold.
11. A system as in Claim 8, further including a floating work platform and means for suspending said manifold and said pump from said platform.
12. A system as in Claim 8, including a plurality of first conduits each connecting an inlet of said first section to one of said chambers and a plurality of second conduits each connecting said second section to one of said bores.
13. A system as in Claim 1, wherein said extending chamber includes a first section extending from said step region and a second inwardly tapered section extending from said first section, said second section being shorter than said first section along the direction of water flow.
14. A system for aerating waste water in a body of waste water comprising:
at least one mixing chamber for providing a waste water passage, including:
an extending chamber, a liquid passage for guiding waste water flow into said extending chamber, the cross-sectional area of passage at the entry to said extending chamber being less than the cross-sectional area of said extending chamber at that entry so as to form a step region, and means defining at least one bore terminating in said step region for injecting gas into said extending chamber, to form parallel gas and water streams, said extending chamber extending downstream from said bore for confining flow of the parallel gas and water streams for a distance until the inter-face between said streams becomes unstable in said extending chamber and vortices are tripped to produce gas bubbles which are mixed with the water stream, at least one helical vane disposed in each said bore for keeping the mixing within said extending chamber, means for pumping said waste water through said at least one mixing chamber, means for mounting said mixing chamber below the surface of said body of water, and means for injecting an aerating gas into waste water within said mixing chamber.
at least one mixing chamber for providing a waste water passage, including:
an extending chamber, a liquid passage for guiding waste water flow into said extending chamber, the cross-sectional area of passage at the entry to said extending chamber being less than the cross-sectional area of said extending chamber at that entry so as to form a step region, and means defining at least one bore terminating in said step region for injecting gas into said extending chamber, to form parallel gas and water streams, said extending chamber extending downstream from said bore for confining flow of the parallel gas and water streams for a distance until the inter-face between said streams becomes unstable in said extending chamber and vortices are tripped to produce gas bubbles which are mixed with the water stream, at least one helical vane disposed in each said bore for keeping the mixing within said extending chamber, means for pumping said waste water through said at least one mixing chamber, means for mounting said mixing chamber below the surface of said body of water, and means for injecting an aerating gas into waste water within said mixing chamber.
15. A mixing chamber for mixing waste water with an aerating gas comprising means defining a passage for waste water flow from an inlet to an outlet, and means forming in said passage an extending chamber with at least one bore opening into said chamber at a step region to inject an aerating gas into said chamber to form parallel streams of gas and water for a distance unti the interface between said streams becomes unstable in said chamber and vortices are tripped to produce gas bubbles which are mixed with the water stream, said extending chamber having at least a portion tapering inwardly in the direction away from said bore to contain the mixing within said chamber.
16. A chamber as in Claim 15, wherein said extending chamber has a first inwardly tapering section extending from said step region and a second section extending from said first section and tapering at a rate greater than the rate of taper of said first section.
17. A chamber as in Claim 15, wherein said bore has a plurality of helical guide vanes for keeping mixing within said chamber.
18. A system for aerating waste water in a body of waste water comprising:
at least one mixing chamber adapted for immersion in said body for providing a waste water passage, including:
an extending chamber;
a liquid passage for guiding waste water flow into said extending chamber, the cross-sectional area of the liquid passage at the entry to said extending chamber being less than the cross-sectional area of said extending chamber at that entry so as to form a step region, and said extending chamber including a first section extending from said step region and a second inwardly tapered section extending from said first section, shorter than said first section along the direction of water flow and tapering inwardly at a rate greater than any inward taper of said first section so as to maintain mixing within said extending chamber over a wide range of gas flow rates; and means defining at least one gas passage terminating in said step region for injecting gas into said extending chamber, to form parallel gas and water streams, said extending chamber extending downstream from said gas passage for confining flow of the parallel gas and water streams for a distance until the interface between said streams becomes unstable in said extending chamber and vortices are tripped to produce gas bubbles which are mixed with the water stream;
means for pumping said waste water through said at least one mixing chamber;
means for mounting said mixing chamber below the surface of said body of water; and means for injecting an aerating gas into waste water within said mixing chamber.
at least one mixing chamber adapted for immersion in said body for providing a waste water passage, including:
an extending chamber;
a liquid passage for guiding waste water flow into said extending chamber, the cross-sectional area of the liquid passage at the entry to said extending chamber being less than the cross-sectional area of said extending chamber at that entry so as to form a step region, and said extending chamber including a first section extending from said step region and a second inwardly tapered section extending from said first section, shorter than said first section along the direction of water flow and tapering inwardly at a rate greater than any inward taper of said first section so as to maintain mixing within said extending chamber over a wide range of gas flow rates; and means defining at least one gas passage terminating in said step region for injecting gas into said extending chamber, to form parallel gas and water streams, said extending chamber extending downstream from said gas passage for confining flow of the parallel gas and water streams for a distance until the interface between said streams becomes unstable in said extending chamber and vortices are tripped to produce gas bubbles which are mixed with the water stream;
means for pumping said waste water through said at least one mixing chamber;
means for mounting said mixing chamber below the surface of said body of water; and means for injecting an aerating gas into waste water within said mixing chamber.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA292,651A CA1088228A (en) | 1977-12-08 | 1977-12-08 | Aeration method and system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA292,651A CA1088228A (en) | 1977-12-08 | 1977-12-08 | Aeration method and system |
Publications (1)
Publication Number | Publication Date |
---|---|
CA1088228A true CA1088228A (en) | 1980-10-21 |
Family
ID=4110236
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CA292,651A Expired CA1088228A (en) | 1977-12-08 | 1977-12-08 | Aeration method and system |
Country Status (1)
Country | Link |
---|---|
CA (1) | CA1088228A (en) |
-
1977
- 1977-12-08 CA CA292,651A patent/CA1088228A/en not_active Expired
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4157304A (en) | Aeration method and system | |
US4244821A (en) | Backflushing system | |
CA1139464A (en) | Multiple stage jet nozzle aeration system | |
US4224158A (en) | Aeration system and method with tapered nozzle | |
US4152259A (en) | Backflushing method | |
US4618426A (en) | Retrievable jet mixing systems | |
KR100239630B1 (en) | Ink Removal Device and Method of Waste Paper Pulp | |
EP0996497A1 (en) | Device and process for liquid treatment | |
US4911836A (en) | Submerged aeration system | |
EP0018374A1 (en) | Water treating device | |
FI96388B (en) | Gas solution and method | |
RU2139131C1 (en) | Reactor | |
JP2012005947A (en) | Pump aeration device | |
CA2222394A1 (en) | A mixing and aeration unit | |
CA1106509A (en) | Aerator | |
CA1088228A (en) | Aeration method and system | |
CA1082375A (en) | Method and system for aeration of waste liquids | |
EP0346109B1 (en) | Device for circulation and gas exchange in liquids | |
CA1088229A (en) | Backflushing method and system | |
EP1478452B1 (en) | Mixing apparatus | |
GB1596190A (en) | Aeration method and apparatus for carrying it out | |
CA1063265A (en) | Liquid aeration device | |
GB1586819A (en) | Backflushing method and apparatus | |
CN208308533U (en) | Aerator and water treatment facilities for water process | |
CN208308532U (en) | Aerator and water treatment facilities for water process |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
MKEX | Expiry |