IP Library Granted Patent US 8,318,016
Granted Patent B1
US 8,318,016 · App. 12/660,206 · Granted Nov 27, 2012

Orbital wastewater treatment system, method of operating same, and kit for modifying an orbital wastewater treatment system

Assignee: Ovivo Luxembourg S.A.R.L.
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Quick Facts
Patent No.
US 8,318,016
App. No.
12/660,206
Granted
Nov 27, 2012
Kind
B1
Abstract

An orbital wastewater treatment system includes a tank assembly, at least one impeller, a flow-diversion mechanism, an actuator, optionally at least one sensor disposed in the tank assembly, and a control unit. The tank assembly has an anoxic zone and an aerobic zone and passages between the two zones. The impeller is disposed in the tank assembly for aeration and for moving mixed liquor under process about the tank assembly. The flow-diversion mechanism is disposed at at least one of the passages between the aerobic and the anoxic zone. The actuator is operatively connected to the gate for regulating the flow state or configuration thereof in response to a signal generated by the control unit at least partially pursuant to a predetermined schedule and/or at least partially in accordance with input from the sensor.

Claims (68)

1. An orbital wastewater treatment system comprising:

a tank assembly having at least a first treatment zone and a second treatment zone, said tank assembly having at least two passages between said first treatment zone and said second treatment zone;

at least one impeller in said tank assembly for moving mixed liquor under process about said tank assembly and through said passages;

a flow-diversion mechanism at at least one of said passages;

an actuator operatively connected to said flow-diversion mechanism;

a control unit operatively connected to said actuator for regulating or adjusting a flow state or configuration of said flow-diversion mechanism; and

at least one selector basin receiving influent and communicating with said first treatment zone.

2. The system defined in claim 1 , further comprising at least one sensor in said at least one selector basin, said control unit being operatively connected to said sensor and said actuator for regulating or adjusting a flow state or configuration of said flow-diversion mechanism at least partially in accordance with input from said sensor.

3. An orbital wastewater treatment system comprising:

a tank assembly having at least a first treatment zone and a second treatment zone, said tank assembly having at least two passages between said first treatment zone and said second treatment zone;

at least one impeller in said tank assembly for moving mixed liquor under process about said tank assembly and through said passages;

a flow-diversion mechanism at at least one of said passages;

an actuator operatively connected to said flow-diversion mechanism;

a control unit operatively connected to said actuator for regulating or adjusting a flow state or configuration of said flow-diversion mechanism;

a mixer disposed in said first treatment zone; and

at least one flow rate sensor for measuring rate of influent flow into said first treatment zone, said control unit being operatively connected to said mixer and said sensor for deactivating or stopping said mixer upon detecting an influent flow rate in excess of a predetermined level.

4. The system defined in claim 3 wherein said control unit is programmed to close said gate upon detecting an influent flow rate in excess of said predetermined level.

5. An orbital wastewater treatment system comprising:

a tank assembly having at least a first treatment zone and a second treatment zone, said tank assembly having at least two passages between said first treatment zone and said second treatment zone;

at least one impeller in said tank assembly for moving mixed liquor under process about said tank assembly and through said passages;

a flow-diversion mechanism at at least one of said passages;

an actuator operatively connected to said flow-diversion mechanism;

a control unit operatively connected to said actuator for regulating or adjusting a flow state or configuration of said flow-diversion mechanism; and

at least one input conduit extending to said tank assembly for delivering recycled activated sludge to at least one of said first treatment zone and said second treatment zone.

6. A method for operating an orbital wastewater treatment system, said system including a tank assembly with at least a first treatment zone and a second treatment zone, said tank assembly including at least two passages between said first treatment zone and said second treatment zone, said method comprising:

energizing at least one impeller in said tank assembly to move mixed liquor about said tank assembly;

automatically adjusting a flow state or configuration of a flow-diversion mechanism at at least one of said passages to modify a flow of mixed liquor between said first treatment zone and said second treatment zone;

measuring a rate of influent flow into said first treatment zone; and

deactivating or stopping a mixer in said first treatment zone upon detecting an influent flow rate in excess of a predetermined level.

7. The method defined in claim 6 , further comprising closing said gate upon detecting an influent flow rate in excess of said predetermined level.

8. A method for operating an orbital wastewater treatment system, said system including a tank assembly with at least a first treatment zone and a second treatment zone, said tank assembly including at least two passages between said first treatment zone and said second treatment zone, said method comprising:

energizing at least one impeller in said tank assembly to move mixed liquor about said tank assembly;

automatically adjusting a flow state or configuration of a flow-diversion mechanism at at least one of said passages to modify a flow of mixed liquor between said first treatment zone and said second treatment zone; and

delivering recycled activated sludge to at least one of said first treatment zone and said second treatment zone,

also comprising automatically operating a sensor at a given location in said tank assembly, the delivering of recycled activated sludge being regulated at least partially in accordance with an output of said sensor.

9. A method for operating an orbital wastewater treatment system, said system including a tank assembly with at least a first treatment zone and a second treatment zone, said tank assembly including at least two passages between said first treatment zone and said second treatment zone, said method comprising:

energizing at least one impeller in said tank assembly to move mixed liquor about said tank assembly; and

automatically adjusting a flow state or configuration of a flow-diversion mechanism at at least one of said passages to modify a flow of mixed liquor between said first treatment zone and said second treatment zone, a mixer being disposed in said first treatment zone and at least one flow rate sensor being provided for measuring rate of influent flow into said first treatment zone, further comprising automatically deactivating or stopping said mixer upon detection by said flow rate sensor of an influent flow rate in excess of a predetermined level.

10. The method defined in claim 9 , further comprising automatically closing said gate upon the detection by said flow rate sensor of an influent flow rate in excess of said predetermined level.

11. A kit for modifying an orbital wastewater treatment tank assembly having at least a first treatment zone and a second treatment zone and further having at least two passages extending between said first treatment zone and said second treatment zone, said kit comprising:

at least one actuator operatively connectable to a flow-diversion mechanism disposed in said tank assembly at at least one of said passages; and

a control unit operatively connectable to said actuator for adjusting or regulating a flow state or configuration of said flow-diversion mechanism.

12. The kit defined in claim 11 , further comprising at least one sensor disposable in said tank assembly, said control unit being operatively connectable to said sensor and said actuator for adjusting or regulating a flow state or configuration of said flow-diversion mechanism at least partially in accordance with input from said sensor.

13. The kit defined in claim 12 wherein said control unit is programmed to adjust said flow-diversion mechanism to one of two opposed extreme states or configurations upon an earlier to occur of (i) a lapse of a predetermined time period after adjusting of said flow-diversion mechanism from said one of said two opposed extreme states or configurations and (ii) a detection by said sensor of a predetermined magnitude of a control parameter in one of said first treatment zone and said second treatment zone.

14. The kit defined in claim 11 wherein said control unit is further programmed to maintain said flow-diversion mechanism in said one of said two opposed extreme states or configurations for a predetermined additional time period and adjust said flow-diversion mechanism from said one of said two opposed extreme states or configurations after termination of said additional time period.

15. The kit defined in claim 11 wherein said control unit is further programmed to periodically adjust said flow-diversion mechanism.

16. The kit defined in claim 13 wherein said control unit is further programmed to adjust said flow-diversion mechanism from said one of said two opposed extreme states or configurations upon an earlier to occur of (i) a lapse of a predetermined additional time period after adjusting of said flow-diversion mechanism to said one of said two opposed extreme states or configurations and (ii) an automated detection of a predetermined magnitude of a preselected control parameter in one of said first treatment zone and said second treatment zone.

17. The kit defined in claim 12 wherein said sensor is taken from the group consisting of a phosphorus (P) sensor, an oxidation reduction potential (ORP) sensor, a dihydride nicotinamide adenine dinucleotide (NADH) sensor, an NO 3 —N sensor, an ammonia (NH 3 —N) sensor, a dissolved oxygen (DO) sensor, and a velocity sensor.

18. The kit defined in claim 12 wherein said sensor is one of a plurality of sensors connectable to said control unit, said sensors further including at least one additional sensor taken from the group consisting of a phosphorus (P) sensor, an oxidation reduction potential (ORP) sensor, a dihydride nicotinamide adenine dinucleotide (NADH) sensor, an NO 3 —N sensor, an ammonia (NH 3 —N) sensor, a dissolved oxygen (DO) sensor, and a velocity sensor.

19. The kit defined in claim 12 wherein said control unit is programmed to maintain said flow-diversion mechanism, upon a closing thereof, in a closed flow state or configuration for a predetermined period of time and to open said flow-diversion mechanism after termination of said period of time.

20. The kit defined in claim 11 , further comprising an additional flow-diversion mechanism operatively connectable to said control unit for regulating flow of recycled activated sludge and influent to said first treatment zone at least partially in accordance with input from said sensor.

21. The kit defined in claim 11 wherein said tank assembly includes at least one impeller in said second treatment zone and at least one mixer in said first treatment zone, said control unit being connectable to said mixer for altering an operating state thereof at least partially in accordance with the flow state or configuration of said flow-diversion mechanism or changes in a sensed process parameter.

22. The kit defined in claim 11 , further comprising at least one flow rate sensor disposable in an influent fee path extending to said first treatment zone, said control unit being operatively connectable to said flow rate sensor, said actuator and a mixer disposed in said first treatment zone, for operating said flow-diversion mechanism to close off flow between said first treatment zone and said second treatment zone and for deactivating said mixer upon detection by said flow rate sensor of an influent flow rate in excess of a predetermined level.

23. An orbital wastewater treatment system comprising:

a tank assembly having at least a first treatment zone and a second treatment zone, said tank assembly having at least two passages between said first treatment zone and said second treatment zone;

at least one impeller for moving mixed liquor under process about said tank assembly and through said passages;

a flow-diversion mechanism at at least one of said passages;

an actuator operatively connected to said flow-diversion mechanism; and

a control unit operatively connected to said actuator for adjusting a flow state or configuration of said flow diversion mechanism.

24. The system defined in claim 23 , further comprising aeration componentry for aerating mixed liquor moving under process about said tank.

25. The system defined in claim 24 wherein said aeration componentry includes said at least one impeller.

26. The system defined in claim 23 , further comprising at least one flow rate sensor disposable in an influent fee path extending to said first treatment zone, said control unit being operatively connectable to said flow rate sensor, said actuator and a mixer disposed in said first treatment zone, for operating said flow-diversion mechanism to close off flow between said first treatment zone and said second treatment zone and for deactivating said mixer upon detection by said flow rate sensor of an influent flow rate in excess of a predetermined level.

27. A method for operating an orbital wastewater treatment system, said system including a tank assembly with at least a first treatment zone and a second treatment zone, said tank assembly including at least two passages between said first treatment zone and said second treatment zone, said method comprising:

moving mixed liquor about said tank assembly; and

automatically adjusting a flow state or configuration of a flow-diversion mechanism at at least one of said passages to modify a flow of mixed liquor between said first treatment zone and said second treatment zone.

28. The method defined in claim 27 wherein the moving said mixed liquid about said tank assembly includes energizing or operating at least one impeller.

29. The method defined in claim 28 wherein said at least one impeller is located in said second treatment zone, at least one mixer being provided in said first treatment zone, further comprising altering an operating state of said mixer at least partially in accordance with the flow state or configuration of said flow-diversion mechanism or changes in a sensed process parameter.

30. The method defined in claim 27 , further comprising aerating the mixed liquor moving about said tank.

Assignments (6)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 27, 2026
From: OVIVO INC.
To: OVIVO WATER INC.
Reel/Frame 074570/0548 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 15, 2016
From: OVIVO FINANCE INC.
To: OVIVO INC.
Reel/Frame 037979/0362 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Mar 2, 2016
From: OVIVO LUXEMBOURG S.À.R.L.
To: OVIVO FINANCE INC.
Reel/Frame 037874/0935 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 16, 2011
From: GLV FINANCE HUNGARY KFT.
To: OVIVO LUXEMBOURG S.A.R.L.
Reel/Frame 026761/0819 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 8, 2010
From: LELAND, THOMAS W.; RISER, FREDERICK M.; REKO, PETER W.
To: GLC FINANCE HUNGARY KFT.
Reel/Frame 024955/0281 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 22, 2010
From: LELAND, THOMAS W.; RISER, FREDERICK M.; REKO, PETER W.
To: GLV FINANCE HUNGARY KFT
Reel/Frame 024032/0430 →
Continuity (2)
Continuation In Part 12321381 · Jan 16, 2009
Provisional Application 61208446 · Feb 23, 2009