Wastewater treatment process

• US 20030042199A1
• Filed: 08/29/2001
• Published: 03/06/2003
• Est. Priority Date: 08/29/2001
• Status: Active Grant

• Current Assignee: Evoqua Water Technologies LLC
• Original Assignee: United States Filter Corporation (Siemens AG)
• Inventors: Smith, George W.
• Granted Patent: US 6,592,762 B2
• Time in Patent Office: Days
• US Class Current: 210/605
• CPC Class Codes: C02F 3/18 the aerator having a horizontal axis
• CPC Class Codes: C02F 3/201 Perforated, resilient plastic diffusers, e.g. membranes, sheets, foils, tubes, hoses
• 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. The process includes introducing 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 mixed liquor is introduced into an oxygen-deficit aeration zone, and denitrified mixed liquor from the oxygen-deficit aeration zone is recycled to the anaerobic zone for mixing therein with wastewater. The process also includes transferring the mixed liquor from the oxygen-deficit aeration zone to an oxygen-surplus aeration zone, transferring a portion of the mixed liquor from the oxygen-surplus aeration zone to a settling zone wherein a supernatant is separated from settled sludge and recycling at least a portion of the settled 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:

introducing wastewater influent into an anaerobic zone having activated sludge;

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

introducing the mixed liquor into an oxygen-deficit aeration zone;

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

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

transferring a portion of the mixed liquor from the oxygen-surplus aeration zone to a settling zone wherein a supernatant is separated from settled sludge; and

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

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 2, wherein the continuous oxygen-deficit aeration zone has a dissolved oxygen concentration of about zero.

4. The process according to claim 1, wherein an aerator device in the oxygen-deficit aeration zone provides oxygen-containing gas and a mixer keeps the mixed liquor in suspension.

5. The process according to claim 4, wherein the aerator device includes a fine bubble membrane diffuser including a flexible membrane having perforations through which the oxygen-containing gas is injected.

6. The process according to claim 4, wherein the aerator device includes aeration discs.

7. The process according to claim 1, wherein the oxygen-surplus aeration zone has a dissolved oxygen concentration of at least about 0.5 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 8, wherein oxygen deficit in the oxygen-deficit aeration zone is produced by supplying atmospheric oxygen at a rate that does not meet oxygen demand therein.

10. The process according to claim 1, wherein the supernatant has a phosphorus concentration of less than 2.5 mg/l.

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

12. A process for treating BOD-containing wastewater using a system employing a plurality of concentric, annular zones, the process comprising:

introducing wastewater influent into an anaerobic zone having activated sludge;

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

introducing the 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 the resulting mixed liquor;

recycling denitrified-mixed liquor from the first aeration zone to the anaerobic zone for mixing therein with wastewater;

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

transferring the mixed liquor from the subsequent aeration zone to a settling zone wherein a supernatant is separated from settled sludge; and

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

13. The process according to claim 12, wherein the overall dissolved oxygen content in the first aeration zone does not exceed about 0.5 mg/l.

14. The process according to claim 12 further comprising recycling a portion of the mixed liquor from the subsequent aeration zone to the first aeration zone for mixing therein with the wastewater and the recycled activated sludge.

15. The process according to claim 12, wherein the subsequent aeration zone comprises:

a second aeration zone maintained under conditions which produce a complete mix reaction and provide sufficient oxygen to produce an overall dissolved oxygen content within the range of about 0.5 to about 1.5 mg/l; and

a third aeration zone, maintained under conditions which produce a complete mix reaction and provide sufficient oxygen to produce an overall dissolved oxygen content of at least 2.0 mg/l in the third aeration zone.

16. The process according to claim 15, further comprising recycling a portion of the mixed liquor from the second aeration zone, the third aeration zone or both the second and third aeration zones to the first aeration zone for mixing therein with the wastewater and the recycled activated sludge.

17. The process to claim 12, wherein the first aeration zone promotes simultaneous nitrification and denitrification.

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

introducing wastewater influent into an anaerobic zone having activated sludge;

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

introducing the mixed liquor into an aerated anoxic zone promoting simultaneous nitrification and denitrification;

recycling denitrified mixed liquor from the aerated anoxic zone to the anaerobic zone for mixing therein with wastewater;

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

transferring the mixed liquor from the subsequent aeration zone to a settling zone wherein supernatant is separated from settled sludge; and

recycling at least a portion of the settled sludge to the aerated anoxic zone.

19. The process of claim 18 further comprising recycling a portion of the mixed liquor from the subsequent aeration zone to the aerated anoxic zone for mixing therein the wastewater and the recycled activated sludge.

20. The process of claim 18, wherein the aerated anoxic zone provides an oxygen deficit by supplying atmospheric oxygen at a rate that does not meet oxygen demand therein.