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

• US 7,510,655 B2
• Filed: 07/13/2007
• Issued: 03/31/2009
• Est. Priority Date: 04/11/2006
• Status: Active Grant

• Current Assignee: Evoqua Water Technologies LLC (Xylem, Inc.)
• Original Assignee: Siemens Water Technologies Corp (Siemens AG)
• Inventors: Barnes, Dennis J.
• Primary Examiner(s): PRINCE JR, FREDDIE GARY
• Application Number:
  US11/777,587
• Publication Number:
  US 20080041783A1
• Time in Patent Office: 627 Days
• Field of Search: 210/605, 210/610, 210/614, 210621-623, 210/630, 210/903, 210/906, 210/908
• US Class Current: 210/605
• CPC Class Codes: C02F 2209/15 N03-N
• CPC Class Codes: C02F 2209/225 in the gas phase
• CPC Class Codes: C02F 2305/06 Nutrients for stimulating the growth of microorganisms
• CPC Class Codes: C02F 3/006 Regulation methods for biological treatment
• 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
• CPC Class Codes: Y10S 210/908 Organic

Abstract

A process for treating BOD, nitrogen and phosphorus containing wastewater, wherein the process includes the steps of providing wastewater influent into an anoxic zone having activated sludge and mixing the wastewater influent with the activated sludge in the anoxic zone to form a mixed liquor. The process further includes providing the mixed liquor into one more further treatment zones and transferring a portion of the mixed liquor from the further treatment zone to a membrane filter wherein a filtrate is separated from sludge. The process also includes selectively recycling at least a portion of the sludge to the anoxic 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 anoxic zone having activated sludge;

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

providing the first mixed liquor into a first of a plurality of further treatment zones;

mixing the first mixed liquor with activated sludge in the first of the plurality of further treatment zones to form a second mixed liquor;

providing the second mixed liquor into a second of the plurality of further treatment zones;

mixing the second mixed liquor with activated sludge in the second of the plurality of further treatment zones to form a third mixed liquor;

providing the third mixed liquor into a third of the plurality of further treatment zones;

mixing the third mixed liquor with activated sludge in the third of the plurality of further treatment zones to form a fourth mixed liquor;

transferring a portion of the fourth mixed liquor from the third of the plurality of further treatment zones to a membrane bioreactor;

filtering the fourth mixed liquor to form a filtrate and an activated sludge; and

selectively recycling at least a portion of the activated sludge from the membrane bioreactor to at least one of the anoxic zone, the first of the plurality of further treatment zones, and the second of the plurality of further treatment zones.

2. The process according to claim 1, wherein the portion of recycled activated sludge includes dissolved oxygen.

3. The process according to claim 2, wherein the dissolved oxygen content of the recycled activated sludge is less than 8 mg/L.

4. The process according to claim 2, wherein the dissolved oxygen content of the recycled activated sludge is in a range of from about 4 mg/L to about 8 mg/L.

5. The process according to claim 1, wherein the anoxic zone promotes simultaneous nitrification and denitrification.

6. The process according to claim 1, further comprising recycling a portion of mixed liquor from the second of the plurality of further treatment zones to the anoxic zone for mixing therein with the wastewater and the recycled activated sludge.

7. The process according to claim 1, wherein one of said plurality of further treatment zones is a further anoxic zone.

8. The process according to claim 7, further comprising providing a source of carbon to the further anoxic zone.

9. The process according to claim 8, further comprising measuring nitrate levels in the filtrate and controlling the source of carbon provided to the further anoxic zone in dependence on the measured nitrate levels.

10. The process of claim 7, wherein the second of the plurality of further treatment zones is an anoxic zone.

11. The process of claim 7, wherein the second of the plurality of further treatment zones is an aerobic zone.

12. The process of claim 1, wherein mixing the wastewater influent with the activated sludge in the anoxic zone comprises mixing the wastewater influent and the activated sludge in the anoxic zone with a mixing device.

13. The process of claim 12, wherein solids are maintained in suspension in the anoxic zone without aeration, the anoxic zone promotes simultaneous nitrification and denitrification, and oxygen utilized for nitrification is provided by the recycled activated sludge.

14. A process for treating BOD, nitrogen and phosphorus containing wastewater, the process comprising the steps of:

providing wastewater influent into a first anoxic zone having activated sludge;

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

transferring at least a portion of the first mixed liquor into an aerobic zone;

mixing the at least a portion of the first mixed liquor with activated sludge in the aerobic zone to form a second mixed liquor;

transferring at least a portion of the second mixed liquor into a second anoxic zone;

mixing the at least a portion of the second mixed liquor with activated sludge in the second anoxic zone to form a third mixed liquor;

transferring at least a portion of the third mixed liquor into a third anoxic zone;

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

transferring a portion of the fourth mixed liquor from the third anoxic zone to a membrane bioreactor;

filtering the portion of the fourth mixed liquor to form a filtrate and an activated sludge; and

selectively recycling at least a portion of the activated sludge to at least one of the first anoxic zone, the aerobic zone, and the second anoxic zone.

15. The process of claim 14, wherein at least one of the first anoxic zone, the second anoxic zone, and the third anoxic zone promotes simultaneous nitrification and denitrification.

16. The process of claim 14, further comprising recycling a portion of mixed liquor from the second anoxic zone to the first anoxic zone for mixing therein with the wastewater and the recycled activated sludge.

17. The process of claim 14, wherein the dissolved oxygen content of the recycled activated sludge is in a range of from about 4 mg/L to about 8 mg/L.

18. The process of claim 14, wherein an oxygen deficit is maintained in the first anoxic zone.

19. The process of claim 18, wherein solids are maintained in suspension in the first anoxic zone without aeration.

20. The process of claim 19, further comprising operating at least one of the second and the third anoxic zone as an aerated anoxic reactor.

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

providing wastewater into an aerobic zone having activated sludge;

mixing the wastewater with the activated sludge in the aerobic zone to form a first mixed liquor having a dissolved oxygen concentration of at least 1 mg/L;

providing a first portion of the first mixed liquor into a first of a plurality of downstream treatment zones;

mixing the first portion of the first mixed liquor with activated sludge in the first of the plurality of downstream treatment zones to form a second mixed liquor;

transferring a portion of the second mixed liquor from the first of the plurality of downstream treatment zones to a membrane bioreactor;

filtering the portion of the second mixed liquor to form a filtrate and 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;

recycling a second portion of the first mixed liquor to a first of a plurality of upstream treatment zones;

recycling a portion of the activated sludge to the first of the plurality of upstream treatment zones;

mixing the second portion of the first mixed liquor, the portion of the activated sludge, and wastewater in the first of the plurality of upstream treatment zones to form a third mixed liquor; and

transferring a portion of the third mixed liquor to a second of the plurality of upstream treatment zones.

22. The process of claim 21, further comprising providing a source of carbon to the first of the plurality of downstream treatment zones.

23. The process of claim 21, wherein mixing the wastewater with the activated sludge comprises mixing the wastewater with the activated sludge using a combination of aerator devices and mechanical mixers.