WO2007112460A1 - Aeration system for tank - Google Patents
Aeration system for tank Download PDFInfo
- Publication number
- WO2007112460A1 WO2007112460A1 PCT/ZA2006/000151 ZA2006000151W WO2007112460A1 WO 2007112460 A1 WO2007112460 A1 WO 2007112460A1 ZA 2006000151 W ZA2006000151 W ZA 2006000151W WO 2007112460 A1 WO2007112460 A1 WO 2007112460A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- tank
- pipe
- liquid
- outlet
- aeration system
- 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.)
- Ceased
Links
Classifications
-
- E—FIXED CONSTRUCTIONS
- E03—WATER SUPPLY; SEWERAGE
- E03F—SEWERS; CESSPOOLS
- E03F5/00—Sewerage structures
- E03F5/18—Tanks for disinfecting, neutralising, or cooling sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/1278—Provisions for mixing or aeration of the mixed liquor
- C02F3/1294—"Venturi" aeration means
-
- Y—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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Definitions
- This invention relates to an aeration system for liquid tanks and in particular sewage tanks.
- the aeration system is not restricted to use in sewage systems and may find a wide range of applications in other tank systems.
- an aeration system for a liquid tank includes an outlet from the tank in communication with a circulating pump, connected to a down-pipe located in the tank via an inlet pipe including an in-line venturi, the down-pipe being vertically orientated and of substantially greater diameter than the inlet pipe and including an outlet located at a low level within the tank, the outlet being adapted to release liquid and entrained air in a substantially horizontal plane, for efficient dispersion throughout the liquid in the tank.
- the down-pipe outlet includes a bend towards a horizontal plane which ensures that the liquid and entrained air is forced into a wide area near the base of the tank.
- the down-pipe outlet includes an elongated substantially horizontal pipe section which is closed along the upper portion thereof, but which includes one or more apertures in the lower portion thereof.
- the horizontal pipe section is cut diagonally from a point near the terminal point of the bend, to a point at or near the end of the horizontal pipe section to form a single, tapered opening in the lower portion thereof.
- the tapered pipe section has several advantages. These include the absence of small apertures which tend to become clogged, but more importantly, it has the effect of forcing the air entrained liquid to be forced horizontally across the diameter of the tank to be dispersed across a much greater area than would be the case if a vertical outlet was used, or even a simple horizontal outlet pipe.
- the system operates by drawing liquid into the pump from the tank and pumping it a sufficient velocity to create a low pressure at the venturi and suck in air.
- Air is entrained in the liquid and passes along the pipe through a bend and into the enlarged vertical down-pipe.
- the air liquid mixture passes down the down-pipe at a velocity which allows some of the entrained bubbles to coalesce and rise up the down- pipe and form an air bubble at the top of the down-pipe.
- four activities take place, namely, transport of entrained air bubbles into the main body of liquid and secondly, coalescing of entrained bubbles which rise up the down-pipe against the flow of liquid.
- An air bubble forms at the top of the down-pipe which is under pressure and the exit flow of the air and gas bubbles is directed into the main body of liquid.
- the system of the invention has several advantages over prior art systems which use air pumps to force pressurised air into liquid tanks. Firstly, liquid pumps are efficient, attain relatively high pressures and are easily obtainable in comparison to air pumps. Secondly, the system utilizes pressure, counter current flows and vigorous mixing to attain rapid and thorough dissolution of air/gas in the liquid. Excellent mixing is obtained because of large flows through the pump. There are no small apertures below the surface in the system, this avoids the problems of clogging of pipes and apertures associated with aeration in biological systems or systems containing sludges etc. The system can be accessed without draining the tanks being aerated.
- a tank 10 is filled with liquid sewage 12 and has an outlet 14 at a high level. Liquid is drawn from the outlet 14 via pipe 16 and using a circulating pump 18. Liquid is pumped through pipe 20 which includes an in-line venturi 22 through which air is drawn into the pipe via air intake 24. The liquid and entrained air enters down-pipe 28 via bend 26.
- the down-pipe 28 has a substantially larger diameter than the pipe 20.
- the down-pipe has an outlet 30 near the base of the tank.
- the outlet includes a bend 32 to the horizontal and an elongated horizontal portion 34 having a tapered opening 36 in the lower portion thereof.
- the air entrained liquid is then dispersed across a wide area at the base of the tank to further increase the efficiency of aeration as the air rises up through the liquid.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Hydrology & Water Resources (AREA)
- Water Supply & Treatment (AREA)
- Health & Medical Sciences (AREA)
- Public Health (AREA)
- Biodiversity & Conservation Biology (AREA)
- Microbiology (AREA)
- Environmental & Geological Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Abstract
An aeration system for liquid tanks, includes an outlet (14) from the tank through which liquid is drawn by a circulating pump (18) to which is connected a down-pipe (28) located in the tank via an inlet pipe (20) which includes an in-line venturi (22) which entrains air in the liquid. The down-pipe (28) is of greater diameter than the inlet pipe (20) and has an outlet (30) at a low-level in the tank which is adapted to release liquid and entrained air in a horizontal plane to ensure efficient dispersion of air throughout the liquid in the tank.
Description
AERATION SYSTEM FOR TANK
TECHNICAL FIELD OF THE INVENTION
This invention relates to an aeration system for liquid tanks and in particular sewage tanks.
BACKGROUND ART
The treatment of sewage requires that it be effectively aerated.
In tanks, it is usually attempted to achieve aeration by pumping pressurised air into the bottom, the air typically entering the tank via a pipe having a large number of small holes at the outlet, or a grating such that a myriad of air bubbles enters the tank and bubble up toward the surface, in so doing aerating the liquid.
This method does not result in satisfactory dissolution of air into the liquid and in addition, problem with the clogging of the outlet are commonly experienced.
It is therefore an object of this invention to provide an aeration system which is more effective than prior art systems.
The aeration system is not restricted to use in sewage systems and may find a wide range of applications in other tank systems.
DISCLOSURE OF THE INVENTION
According to the invention an aeration system for a liquid tank includes an outlet from the tank in communication with a circulating pump, connected to a down-pipe located in the tank via an inlet pipe including an in-line venturi, the down-pipe being vertically orientated and of substantially greater diameter than the inlet pipe and including an outlet located at a low level within the tank, the outlet being adapted to
release liquid and entrained air in a substantially horizontal plane, for efficient dispersion throughout the liquid in the tank.
In the preferred form of the invention, the down-pipe outlet includes a bend towards a horizontal plane which ensures that the liquid and entrained air is forced into a wide area near the base of the tank.
Also in the preferred form the down-pipe outlet includes an elongated substantially horizontal pipe section which is closed along the upper portion thereof, but which includes one or more apertures in the lower portion thereof. In the preferred form the horizontal pipe section is cut diagonally from a point near the terminal point of the bend, to a point at or near the end of the horizontal pipe section to form a single, tapered opening in the lower portion thereof.
The tapered pipe section has several advantages. These include the absence of small apertures which tend to become clogged, but more importantly, it has the effect of forcing the air entrained liquid to be forced horizontally across the diameter of the tank to be dispersed across a much greater area than would be the case if a vertical outlet was used, or even a simple horizontal outlet pipe.
In operation, the system operates by drawing liquid into the pump from the tank and pumping it a sufficient velocity to create a low pressure at the venturi and suck in air. Air is entrained in the liquid and passes along the pipe through a bend and into the enlarged vertical down-pipe. The air liquid mixture passes down the down-pipe at a velocity which allows some of the entrained bubbles to coalesce and rise up the down- pipe and form an air bubble at the top of the down-pipe. Thus in the down-pipe, four activities take place, namely, transport of entrained air bubbles into the main body of liquid and secondly, coalescing of entrained bubbles which rise up the down-pipe against the flow of liquid. An air bubble forms at the top of the down-pipe which is under pressure and the exit flow of the air and gas bubbles is directed into the main body of liquid.
These activities all assist in ensuring enhanced aeration and mixing.
The efficiency of the system in dissolving air in the liquid is dependent upon the following factors:
1. The velocity of the liquid through the venturi
2. The size of the pipe and venturi in relation to the pump
3. The depth of the vertical enlarged section, and therefore the back pressure in the enlarged section
4. The velocity of the liquid/gas mixture in the vertical enlarged section. This is related to the pump and the diameter of the enlarged section.
The system of the invention has several advantages over prior art systems which use air pumps to force pressurised air into liquid tanks. Firstly, liquid pumps are efficient, attain relatively high pressures and are easily obtainable in comparison to air pumps. Secondly, the system utilizes pressure, counter current flows and vigorous mixing to attain rapid and thorough dissolution of air/gas in the liquid. Excellent mixing is obtained because of large flows through the pump. There are no small apertures below the surface in the system, this avoids the problems of clogging of pipes and apertures associated with aeration in biological systems or systems containing sludges etc. The system can be accessed without draining the tanks being aerated.
BRIEF DESCRIPTION OF THE DRAWINGS
An embodiment of the invention is described below with reference to the accompanying drawing which is a sectional view through a tank having its contents aerated using the system of the invention.
BEST MODE FOR CARRYING OUT THE INVENTION
In the drawings, a tank 10 is filled with liquid sewage 12 and has an outlet 14 at a high level. Liquid is drawn from the outlet 14 via pipe 16 and using a circulating pump 18. Liquid is pumped through pipe 20 which includes an in-line venturi 22 through which air is drawn into the pipe via air intake 24. The liquid and entrained air enters down-pipe 28 via bend 26.
The down-pipe 28 has a substantially larger diameter than the pipe 20. The down-pipe has an outlet 30 near the base of the tank. The outlet includes a bend 32 to the horizontal and an elongated horizontal portion 34 having a tapered opening 36 in the lower portion thereof.
Air bubbles coalesce in the down-pipe and rise up it to form a bubble at the top 38 through which the incoming liquid must travel. This enhances dissolution. The air entrained liquid is then dispersed across a wide area at the base of the tank to further increase the efficiency of aeration as the air rises up through the liquid.
Claims
1. An aeration system for a liquid tank characterised in that the system includes an outlet from the tank in communication with a circulating pump, connected to a down-pipe located in the tank via an inlet pipe including an in-line venturi, the down-pipe being vertically orientated and of substantially greater diameter than the inlet pipe and including an outlet located at a low level within the tank, the outlet being adapted to release liquid and entrained air in a substantially horizontal plane, for efficient dispersion throughout the liquid in the tank.
2. An aeration system according to claim 1 characterised in that the down-pipe outlet includes a bend towards a horizontal plane which ensures that the liquid and entrained air is forced into a wide area near the base of the tank.
3. An aeration system according to claim 1 or claim 2 characterised in that the down-pipe outlet includes an elongated substantially horizontal pipe section which is closed along the upper portion thereof, but which includes one or more apertures in the lower portion thereof.
4. An aeration system according to claim 3 characterised in that the horizontal pipe section is cut diagonally from a point near the terminal point of the bend, to a point at or near the end of the horizontal pipe section to form a single, tapered opening in the lower portion thereof.
5. An aeration system according to any of the above claims substantially as described with reference to the accompanying drawings.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AP2008004688A AP2604A (en) | 2006-03-28 | 2006-12-21 | Aeration system for tank |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| ZA200602524 | 2006-03-28 | ||
| ZA2006/02524 | 2006-03-28 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2007112460A1 true WO2007112460A1 (en) | 2007-10-04 |
Family
ID=37998705
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/ZA2006/000151 Ceased WO2007112460A1 (en) | 2006-03-28 | 2006-12-21 | Aeration system for tank |
Country Status (3)
| Country | Link |
|---|---|
| AP (1) | AP2604A (en) |
| WO (1) | WO2007112460A1 (en) |
| ZA (1) | ZA200805931B (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2241337A (en) * | 1939-03-04 | 1941-05-06 | Beaton & Cadwell Mfg Company | Liquid agitating and siphon break apparatus |
| GB1163780A (en) * | 1965-12-16 | 1969-09-10 | Kloeckner Humboldt Deutz Ag | Apparatus for biological clarification of waste-water |
| FR2156376A2 (en) * | 1969-05-08 | 1973-05-25 | Basf Ag | Aerator |
| US4072612A (en) * | 1976-05-25 | 1978-02-07 | Daniel William H | Aerator for bodies of water |
-
2006
- 2006-12-21 WO PCT/ZA2006/000151 patent/WO2007112460A1/en not_active Ceased
- 2006-12-21 AP AP2008004688A patent/AP2604A/en active
-
2008
- 2008-07-08 ZA ZA200805931A patent/ZA200805931B/en unknown
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2241337A (en) * | 1939-03-04 | 1941-05-06 | Beaton & Cadwell Mfg Company | Liquid agitating and siphon break apparatus |
| GB1163780A (en) * | 1965-12-16 | 1969-09-10 | Kloeckner Humboldt Deutz Ag | Apparatus for biological clarification of waste-water |
| FR2156376A2 (en) * | 1969-05-08 | 1973-05-25 | Basf Ag | Aerator |
| US4072612A (en) * | 1976-05-25 | 1978-02-07 | Daniel William H | Aerator for bodies of water |
Also Published As
| Publication number | Publication date |
|---|---|
| AP2008004688A0 (en) | 2008-12-31 |
| ZA200805931B (en) | 2010-05-26 |
| AP2604A (en) | 2013-02-27 |
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