MICROBUBBLE AERATOR
20180134596 ยท 2018-05-17
Inventors
Cpc classification
C02F3/1278
CHEMISTRY; METALLURGY
Y02W10/37
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
B01F23/23231
PERFORMING OPERATIONS; TRANSPORTING
Y02W10/10
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
B01F2101/305
PERFORMING OPERATIONS; TRANSPORTING
B01F33/5023
PERFORMING OPERATIONS; TRANSPORTING
International classification
Abstract
An aerating system for treating a waste lagoon or some type of wastewater that captures and recirculates air that has been previously pumped into the lagoon via a skirt. The system also utilizes an oxygen source to pump oxygen into the waste lagoon or wastewater that can also be recirculated. A manifold of the system is designed to have intakes for both the recirculated air and for the oxygen source.
Claims
1. An aerating system for a waste lagoon, comprising: a means for creating a pressure gradient; a flotation member; an exit channel having a first pressure within; wherein the means for creating a pressure gradient directs air into the waste lagoon via the exit channel; a manifold connected to the exit channel; the manifold having a first intake member; a skirt extending laterally from the flotation member; a chamber between the skirt and the flotation member; a passageway between the chamber and the first intake member; wherein air in the chamber is circulated into the air pump via the first intake member.
2. The aerating system of claim 1, further comprising: a second intake member; the second intake member connected to the chamber; wherein air in the chamber is circulated into the air pump via the second intake member and the first intake member.
3. The aerating system of claim 2, wherein: the manifold comprises a third intake member; wherein an oxygen source is connected to the third intake member; wherein oxygen is circulated into the air pump via the third intake member.
4. The aerating system of claim 3, further comprising: at least one seal; wherein the seal is between the skirt and the flotation member and maintains an airtight seal.
5. The aerating system of claim 4, wherein: the skirt comprises a wall extending vertically past the flotation member.
6. The aerating system of claim 5, wherein: the manifold further comprises a fourth intake member; wherein the oxygen source is connected to the fourth intake member.
7. The aerating system of claim 6, wherein: a portion of the air pumped through the exit channel resurfaces in the chamber.
8. The aerating system of claim 7, wherein: the portion of the air is recirculated via the aerating system and the system creates smaller bubbles of air; whereby a portion of the recirculated air contains microbubbles that dissolve in the lagoon rather than resurface.
9. The aerating system of claim 8, further comprising: at least one solar panel.
10. The aerating system of claim 9, wherein: the oxygen source is an oxygenator.
11. An aerating system for treating wastewater, comprising: an air pump; a flotation member; an exit channel; wherein the air pump directs air into the wastewater via the exit channel; a manifold connected to the air pump; the manifold having a first intake member; a passageway between the first intake member and an oxygen source; wherein oxygen is circulated into the air pump via the first intake member.
12. The aerating system of claim 11, further comprising: a skirt extending laterally from the flotation member; a chamber between the skirt and the flotation member; a second passageway between the chamber and a second intake member; wherein air in the chamber is circulated into the air pump via the second intake member.
13. The aerating system of claim 12, further comprising: at least one seal; wherein the seal is between the skirt and the flotation member and maintains an airtight seal.
14. The aerating system of claim 13, wherein: the skirt comprises a wall extending vertically past the flotation member.
15. The aerating system of claim 14, wherein: a portion of the air pumped through the exit channel resurfaces in the chamber.
16. The aerating system of claim 15, wherein: the portion of the air is recirculated via the aerating system and the system creates smaller bubbles of air; whereby a portion of the recirculated air contains microbubble that dissolve in the lagoon rather than resurface.
17. The aerating system of claim 16, further comprising: at least one solar panel.
18. The aerating system of claim 17, wherein: the oxygen source is an oxygenator.
19. An aerating system for treating wastewater, comprising: a water pump; a tank for holding a liquid; wherein the water pumps wastewater from a first location to the tank; an air pump; wherein the air pump directs air into the liquid of the tank; an oxygen source; wherein oxygen is directed into the liquid of the tank; the tank comprising an output member wherein the liquid exits the tank; a linkage member connecting the output member to the first location of the wastewater; wherein the wastewater is pumped from the first location to the tank and then back to the first location; a manifold connected to the tank; the manifold having a first intake member; wherein the oxygen source is connected to the first intake member; wherein oxygen is circulated into the tank via the first intake member.
Description
BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWING(S)
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DETAILED DESCRIPTION OF THE INVENTION
[0017]
[0018] A chamber 34 is formed between the descending wall 30 and a side 36 of the flotation member 24. As the preferred embodiment has a flotation member 24 and skirt 26 that are rectangular, the preferred embodiment has a chamber 34 that is present on all four sides of the flotation member 24. At least one seal 38 is positioned between the upper portion 28 of the skirt 26 and a top 40 of the flotation member 24 in order to maintain an airtight seal.
[0019] As shown in
[0020] As best seen in
[0021]
[0022]
[0023] In operation of the preferred embodiment, the motor 22 is connected to a power source and turned on. As the motor 22 powers a means to lower the air pressure in the exit channel 72, the recirculated air and oxygen from the oxygen source is drawn through the openings 73 in the base 68 and directed downward via the exit channel 72 and into the liquid to be treated by the system 20. The air pressures involved allow air trapped in the chamber 34 and oxygen from the oxygen source to be forced into the exit channel 72 via the manifold 50. As the system 20 runs, a portion of the air and oxygen that is pumped into the liquid (such as a waste lagoon) will resurface to the surface of the liquid. Furthermore, a portion of the resurfacing air and oxygen will resurface within the chamber 34. The air and oxygen resurfacing in the chamber 34 will be forced through the passageways 58 that lead from the skirt 26 to the intake members 54 and 56. That air and oxygen is then forced downward again and the process repeats itself. Oxygen is also fed to the manifold 50 via passageways 58 that lead from the oxygen source 64 to the intake members 60 and 62. The oxygen can be metered to control the flow and use of the amount of oxygen by the system 20. Additionally, a side of the skirt could be fitted with a hinge that allows the top of the skirt to open when a certain predetermined air pressure is exceeded in the chamber, basically allowing the system to burp itself.
[0024] Testing of the system 20 on a waste lagoon indicates a significant increase in the oxygen content of the liquid. In testing, a 3000 gallon pool had a beginning dissolved oxygen content of zero parts per million (ppm). After running the system without an oxygen source for ninety minutes, the dissolved oxygen content was 8 ppm. A similar test, this time with an oxygen source brought the dissolved oxygen content to 8 ppm in only ten minutes and reached 20 ppm in thirty minutes. The reason is that more microbubbles can be produced by the system 20 and the microbubbles do not resurface, rather they stay within the liquid being treated and are available for microorganisms in the liquid being treated. The increased oxygen content means that less aeration systems are needed on a particular waste lagoon or wastewater. Initial testing indicates that the number of systems could be cut by 80 percent. For example, a waste lagoon requiring thirty prior art aeration systems could be treated by six of the aerating systems 20. The use of fewer systems saves costs to the end user in terms of the number of units needed to be purchased as well as savings in electrical costs.
[0025] A third embodiment of the invention is detailed in
[0026] The aerating system 220 utilizes a similar motor and manifold system as the ones described in the other embodiments. Specifically, the system 220 further comprises a motor 250 mounted on a base 252. An exit channel 254 is located on the opposite side of the base than the motor 250. A manifold 256 is mounted on the base 252 and preferably has a plurality of intake members 258. Similar to the previous embodiments, the intake members 258 can bring oxygen and recirculated air back to the exit channel 254 and thus into the liquid in the tank 221. The confined tank 221 acts as the skirt of the other embodiments.
[0027] In operation, liquid from the wastewater source is pumped into the tank 221. At the same time, the motor 250 pumps air through the exit channel 254 and into the liquid contained in the tank 221. As some of the air pumped into the tank 221 rises, it exits a third opening 270 of the tank 221 and goes through a passageway 272 that leads to an intake member 258 of the manifold 256. The manifold 256 then is in communication with the exit channel 254 such that the air can be recirculated into the liquid. Preferably, an oxygen source 280 is connected to a second intake member 290 of the manifold 256 such that oxygen can be supplied to the system. A portion of the liquid in the tank 221 exits through the second opening 224 and is returned to the wastewater source. As in the other embodiments, variable numbers of intake members can be utilized in the third embodiment.
[0028] The foregoing description of the invention has been presented for purposes of illustration and description and is not intended to be exhaustive or to limit the invention to the precise form disclosed. Modifications and variations of the embodiments are possible in light of the above disclosure or such may be acquired through practice of the invention. The embodiments illustrated were chosen in order to explain the principles of the invention and its practical application to enable one skilled in the art to utilize the invention in various embodiments and with various modifications as are suited to the particular use contemplated. It is intended that the scope of the invention be defined by the claims appended hereto, and by their equivalents.