Sludge digestion methods and apparatus

• US 6,869,534 B2
• Filed: 05/05/2003
• Issued: 03/22/2005
• Est. Priority Date: 05/05/2002
• Status: Expired due to Fees

• Current Assignee: Brentwood Industries, Incorporated
• Original Assignee: Brentwood Industries, Incorporated
• Inventors: Maurer, Robert, Hannum, Chris, McDowell, Curtis S.
• Primary Examiner(s): Barry, Chester T.
• Application Number:
  US10/430,171
• Publication Number:
  US 20040011737A1
• Time in Patent Office: 687 Days
• Field of Search: 210/220, 210/739, 210/745, 210/195.1, 210/97, 210/620
• US Class Current: 210/620
• CPC Class Codes: C02F 2209/10 Solids, e.g. total solids [TS], total suspended solids [TSS] or volatile solids [VS]
• CPC Class Codes: C02F 2209/42 Liquid level
• CPC Class Codes: C02F 3/006 Regulation methods for biological treatment
• CPC Class Codes: C02F 3/1284 Mixing devices
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage

Abstract

The invention relates to an aerobic wastewater digestion unit useful for degrading organic material dissolved or suspended in a wastewater stream. The wastewater is fed to a vessel, wherein it is circulated by a liquid conveyor between the vessel and a downwardly-directed tube. Expulsion of fluid from the tube into the lower portion of the vessel agitates the liquid in the vessel and disperses into the liquid air that has been entrained in the liquid in the tube. The digester can be operated using varying liquid levels, and is amenable to batch, semi-batch, and continuous operation. The digester is suitable for use in combination with other components of wastewater treatment systems, and can be included as a module in modular wastewater treatment systems.

Claims

1. An aerobic digester for organic material comprising:

a vessel for containing a liquid comprising the organic material, the vessel having an interior comprising an upper portion, a lower portion and a lower interior surface;

a tube having a distal end disposed in the lower portion of the interior of the vessel, an opening in a wall of the tube for permitting liquid and air flow between an exterior and an interior of the tube, and at least one discharge port disposed in the distal end; and

a liquid conveyor connected in fluid communication with the interior of the tube for inducing flow of the liquid along the tube in the direction of the distal end,

whereby the liquid conveyor induces entrainment of air drawn into the tube through the opening into the liquid drawn into the tube through the opening to form a liquid-air mixture and expulsion of the liquid-air mixture from the tube through the at least one discharge port into the lower portion of the vessel, thereby causing liquid contained in the vessel to be mixed and aerated.

2. The digester of claim 1, wherein the liquid conveyor is at least partially disposed within the tube.

3. The digester of claim 2, wherein the liquid conveyor comprises a motor having a shaft rotatably connected thereto, the shaft having at least one impeller attached thereto and being disposed within the tube.

4. The digester of claim 3, wherein the impeller is disposed within the interior of the tube at a level below a lowermost level of the opening.

5. The digester of claim 4, wherein the tube comprises at least two openings spaced along the length of the tube and the liquid conveyor comprises at least two impellers, each of the impellers being disposed below a different opening.

6. The digester of claim 5, wherein the tube comprises an upper opening, an intermediate opening distally disposed along the length of the tube below the upper opening, and a lower opening distally disposed along the length of the tube below the intermediate opening, and whereby the liquid conveyor comprises an upper impeller disposed below the intermediate opening, but above the lower opening, and a lower impeller disposed below the lower opening.

7. The digester of claim 6, wherein air enters the tube through the upper opening.

8. The digester of claim 7, wherein liquid enters the tube through the intermediate and lower openings.

9. The digester of claim 8, wherein liquid in the vessel is maintained at a level between the upper and intermediate openings.

10. The digester of claim 1, wherein air is supplied to the upper portion of the vessel by a fan.

11. The digester of claim 1, wherein the tube has an internal baffle extending along at least a portion of a length of the tube for reducing liquid flow in directions not parallel with a longitudinal axis of the tube.

12. The digester of claim 1, wherein the tube is oriented substantially vertically.

13. The digester of claim 1, wherein the tube has a substantially constant diameter along its length.

14. The digester of claim 1, wherein the tube has a substantially circular cross-section along its entire length.

15. The digester of claim 1, wherein the tube is fixed to the lower interior surface of the vessel.

16. The digester of claim 14, wherein the liquid conveyor comprises a rotating shaft rotatably supported in a shaft support.

17. The digester of claim 1, wherein the opening extends through about 10% to about 20% of the circumference of the tube.

18. The digester of claim 1, wherein the opening extends through at least about 20% of the circumference of the tube.

19. The digester of claim 1, wherein the opening is dimensioned such that the area of the opening is about 10% to about 20% of the cross-sectional area of the tube at a lowermost level of the opening.

20. The digester of claim 1, wherein the opening is positioned axially along the tube such that the surface of liquid in the vessel is within the opening during operation of the digester.

21. The digester of claim 1, further comprising a liquid inlet for providing liquid to the interior of the vessel.

22. The digester of claim 21, wherein the liquid inlet discharges liquid into the lower portion of the interior of the vessel.

23. The digester of claim 21, wherein the liquid inlet is in fluid communication with the solids discharge outlet of a wastewater primary clarifying apparatus.

24. The digester of claim 1, further comprising a liquid outlet for discharging liquid from the interior of the vessel.

25. The digester of claim 24, wherein the liquid outlet is in fluid communication with a decant weir having an opening disposed at or near the upper surface of the liquid in the vessel, for withdrawing liquid from or near the upper surface of the liquid and delivering the withdrawn liquid to the liquid outlet.

26. The digester of claim 25, wherein the decant weir is fixed in the interior of the vessel, whereby the decant weir maintains a maximum liquid depth in the vessel.

27. The digester of claim 25, wherein the decant weir is vertically movably disposed in the interior of the vessel with respect to the upper surface of the liquid.

28. The digester of claim 24, wherein a bulk fluid flow baffle is interposed between the distal end of the tube and the liquid outlet, whereby the bulk fluid flow baffle inhibits withdrawal from the vessel of solids suspended in the liquid.

29. The digester of claim 24, further comprising a suspended solids sensor in sensory communication with liquid in the vessel.

30. The digester of claim 29, wherein the sensor is a turbidity sensor.

31. The digester of claim 29, wherein the sensor is a viscosity sensor.

32. The digester of claim 29, further comprising an alarm in signaling communication with the sensor, for indicating when the level of suspended solids in liquid in the liquid outlet exceeds a selected value.

33. The digester of claim 29, further comprising a solids disposal outlet in fluid communication with a flow regulator that is in fluid communication with the lower portion of the interior of the vessel and in signaling communication with the sensor, whereby the flow regulator permits withdrawal of liquid and residual sludge from the vessel by way of the solids disposal outlet when the level of suspended solids in liquid in the liquid outlet exceeds a selected value.

34. The digester of claim 1, further comprising a solids disposal outlet in fluid communication with the lower portion of the interior of the vessel.

35. The digester of claim 34, wherein the solids disposal outlet is in fluid communication with a sludge holding tank.

36. The digester of claim 34, wherein the solids disposal outlet is in fluid communication with a solids filter for separating liquid withdrawn from the vessel into filtered solids and solids filtrate fractions.

37. The digester of claim 36, further comprising a return line for returning the solids filtrate to a biological reactor.

38. The digester of claim 34, wherein a flow regulator is disposed in a discharge line extending from the solids disposal outlet.

39. The digester of claim 38, wherein the regulator is a valve.

40. The digester of claim 38, wherein the regulator is a pump.

41. A wastewater treatment system comprising a primary clarifier for removing bulk solids from a wastewater stream, the primary clarifier being upstream from a biological reactor for degrading an organic material in the stream, the reactor being upstream from a secondary clarifier for removing solids from a post-reactor waste-stream, and the digester of claim 1 being in fluid communication with a solids discharge outlet of one or both of the primary clarifier and the secondary clarifier.

42. The system of claim 41, wherein a single pump selectably connected with multiple fluid circuits drives fluid flow between the primary clarifier, the biological reactor, the secondary clarifier, and the digester of claim 1.

43. The system of claim 42, wherein separate pumps are selectably connected with multiple fluid circuits and drive fluid flow between the primary clarifier, the biological reactor, the secondary clarifier, and the digester of claim 1.

44. A method of aerobically digesting organic material in wastewater, the method comprising the steps of:

a) providing the wastewater comprising the organic material to a digester that comprises;

a vessel for containing a liquid, the vessel having an interior comprising an upper portion and a lower portion and a lower interior surface;

a tube having a distal end disposed in the lower portion of the interior of the vessel, an opening in the wall of the tube for permitting liquid and air flow between the exterior and interior of the tube, and at least one discharge port disposed in the distal end; and

a liquid conveyor disposed within the tube for inducing flow of the liquid through the tube in the direction of the distal end, the conveyor comprising an impeller disposed below the opening; and

b) circulating the liquid in the digester by way of the tube, whereby the conveyor induces entrainment of air into the liquid drawn into the tube by way of the opening to form a liquid-air mixture and expulsion of the liquid-air mixture from the tube through the at least one discharge port, thereby inducing mixing and aeration of the liquid in the vessel and digesting organic material in the wastewater.

45. The method of claim 44, further comprising the step of operating the liquid conveyor for a predetermined period.

46. The method of claim 45, further comprising the step of discontinuing operation of the liquid conveyor to allow gravity sedimentation of solids in the wastewater for a predetermined period.

47. The method of claim 46, further comprising the step of testing the clarity of the liquid in the vessel at a predetermined position within the vessel.

48. The method of claim 47, further comprising the step of withdrawing liquid from a lower portion of the vessel if the clarity is below a predetermined level.

49. The method of claim 48, further comprising the step of withdrawing liquid from an upper portion of the vessel if the clarity is above a predetermined level.