Process to improve the efficiency of a membrane filter activated sludge system

• US 7,481,933 B2
• Filed: 04/11/2006
• Issued: 01/27/2009
• Est. Priority Date: 04/11/2006
• Status: Active Grant

• Current Assignee: Evoqua Water Technologies LLC
• Original Assignee: Siemen Water Technologies Corporation (Siemens AG)
• Inventors: Barnes, Dennis J.
• Primary Examiner(s): PRINCE JR, FREDDIE GARY
• Application Number:
  US11/279,354
• Publication Number:
  US 20070235386A1
• Time in Patent Office: 1,022 Days
• Field of Search: 210/605, 210/610, 210621-623, 210/903, 210/906, 210/908
• US Class Current: 210/605
• CPC Class Codes: C02F 3/1268 Membrane bioreactor systems
• CPC Class Codes: C02F 3/308 Biological phosphorus removal
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage
• CPC Class Codes: Y10S 210/903 Nitrogenous
• CPC Class Codes: Y10S 210/906 Phosphorus containing

Abstract

A process for treating BOD, nitrogen and phosphorus containing wastewater, wherein the process includes providing wastewater influent into an anaerobic zone having activated sludge and mixing the wastewater influent with the activated sludge in the anaerobic zone to form a mixed liquor. The process further includes providing the mixed liquor into an oxygen-deficit aeration zone and recycling denitrified mixed liquor from the oxygen-deficit aeration zone to the anaerobic zone for mixing therein with wastewater. In addition, the process includes transferring the mixed liquor from the oxygen-deficit aeration zone to an oxygen-surplus aeration zone and transferring a portion of the mixed liquor from the oxygen-surplus aeration zone to a membrane filter wherein a filtrate is separated from sludge. The process also includes recycling at least a portion of the sludge to the oxygen-deficit aeration zone as recycled activated sludge.

Claims

1. A process for treating BOD, nitrogen and phosphorus containing wastewater, the process comprising:

providing wastewater influent into an anaerobic zone having activated sludge;

mixing the wastewater influent with the activated sludge in the anaerobic zone to form a first mixed liquor;

providing the first mixed liquor into an oxygen-deficit aeration zone;

mixing the first mixed liquor with activated sludge in the oxygen-deficit aeration zone to form a denitrified mixed liquor;

recycling a portion of the denitrified mixed liquor from the oxygen-deficit aeration zone to the anaerobic zone for mixing therein with the wastewater influent;

transferring the denitrified mixed liquor from the oxygen-deficit aeration zone to an oxygen-surplus aeration zone;

mixing the denitrified mixed liquor with activated sludge in the oxygen-surplus aeration zone to form a third mixed liquor;

transferring a portion of the third mixed liquor from the oxygen-surplus aeration zone to a membrane bioreactor wherein a filtrate is separated from a sludge;

providing oxygen to the membrane bioreactor;

introducing oxygen provided to the membrane bioreactor into the sludge to form an activated sludge with a dissolved oxygen level of between about 4 mg/L and about 8 mg/L; and

recycling at least a portion of the activated sludge to the oxygen-deficit aeration zone.

2. The process according to claim 1, wherein oxygen deficit in the oxygen-deficit aeration zone is maintained by controlling aeration so that oxygen supply is less than oxygen consumption by microorganisms therein.

3. The process according to claim 1, wherein an aerator device in the oxygen-deficit aeration zone provides at least some oxygen-containing gas and mixing energy to keep the mixed liquor in suspension.

4. The process of claim 3, further comprising maintaining mixed liquor solids in suspension in the oxygen-deficit aeration zone using a combination of aerator devices and mechanical mixers.

5. The process according to claim 1, wherein the third mixed liquor has a dissolved oxygen concentration of at least about 0.5 mg/L.

6. The process according to claim 5, wherein the third mixed liquor has a dissolved oxygen concentration of at least 1 mg/L.

7. The process according to claim 6, wherein the third mixed liquor has a dissolved oxygen concentration of at least 5 mg/L.

8. The process according to claim 1, wherein in the oxygen-deficit aeration zone promotes simultaneous nitrification and denitrification.

9. The process according to claim 1, further comprising recycling a portion of the third mixed liquor from the oxygen-surplus aeration zone to the oxygen-deficit aeration zone for mixing therein with the first mixed liquor and the recycled activated sludge.

10. The process of claim 1, wherein the oxygen is introduced into the membrane bioreactor in the form of air.

11. A process for treating BOD, nitrogen and phosphorus containing wastewater, the process comprising:

providing wastewater influent into an anaerobic zone having activated sludge;

mixing the wastewater influent with the activated sludge to form a first mixed liquor;

providing the first mixed liquor into a first aeration zone maintained under conditions which produce a complete mix reaction and provide insufficient oxygen to meet the biological oxygen demand of a resulting denitrified mixed liquor;

recycling a portion of the denitrified mixed liquor from the first aeration zone to the anaerobic zone for mixing therein with the wastewater influent;

transferring the denitrified mixed liquor to a subsequent aeration zone under conditions which produce a complete mix reaction and provide sufficient oxygen to produce a third mixed liquor with an overall dissolved oxygen content of at least 0.5 mg/L;

transferring the third mixed liquor from the subsequent aeration zone to a membrane bioreactor wherein a filtrate is separated from a sludge;

providing oxygen to the membrane bioreactor;

introducing oxygen provided to the membrane bioreactor into the sludge to form an activated sludge with a dissolved oxygen level of between about 4 mg/L and about 8 mg/L; and

recycling at least a portion of the activated sludge to the first aeration zone.

12. The process of claim 11 further comprising recycling a portion of third mixed liquor to the first aeration zone for mixing therein the first mixed liquor and the recycled activated sludge.

13. A process for treating BOD, nitrogen and phosphorus containing wastewater, the process comprising:

providing wastewater influent into an anaerobic zone having activated sludge;

mixing the wastewater influent with the activated sludge in the anaerobic zone to form a first mixed liquor;

providing the first mixed liquor into an oxygen-deficit aeration zone;

mixing the first mixed liquor with activated sludge in the oxygen-deficit aeration zone to form a denitrified mixed liquor;

recycling a portion of the denitrified mixed liquor from the oxygen-deficit aeration zone to the anaerobic zone for mixing therein with the wastewater influent;

transferring the denitrified mixed liquor from the oxygen-deficit aeration zone to an oxygen-surplus aeration zone;

mixing the denitrified mixed liquor with activated sludge in the oxygen-surplus aeration zone to form a third mixed liquor;

transferring the third mixed liquor from the oxygen-surplus aeration zone to an anoxic zone;

mixing the third mixed liquor with activated sludge in the anoxic zone to form a fourth mixed liquor;

transferring a portion of the fourth mixed liquor from the anoxic zone to a membrane bioreactor wherein a filtrate is separated from a sludge;

providing oxygen to the membrane bioreactor;

introducing oxygen provided to the membrane bioreactor into the sludge to form an activated sludge with a dissolved oxygen level between about 4 mg/L and about 8 mg/L; and

recycling at least a portion of the activated sludge to the oxygen-deficit aeration zone.

14. The process according to claim 13, further comprising providing a source of carbon to the anoxic zone to assist denitrification.

15. The process of claim 13, further comprising recycling a portion of the third mixed liquor to the first aeration zone for mixing therein the first mixed liquor and the recycled activated sludge.

16. The process of claim 13, wherein the dissolved oxygen content of the third mixed liquor is above 5 mg/L.

17. The process according to claim 13, wherein in the oxygen-deficit aeration zone promotes simultaneous nitrification and denitrification.

18. The process of claim 17, further comprising maintaining mixed liquor solids in suspension in the oxygen-deficit aeration zone using a combination of aerator devices and mechanical mixers.

19. The process of claim 13, wherein oxygen deficit in the oxygen-deficit aeration zone is maintained by controlling aeration so that oxygen supply is less than oxygen consumption by microorganisms therein.

20. The process of claim 13, wherein an aerator device in the oxygen-deficit aeration zone provides at least some oxygen-containing gas and mixing energy to keep the mixed liquor in suspension.