Wastewater treatment method and plant

• US 5,961,830 A
• Filed: 05/13/1997
• Issued: 10/05/1999
• Est. Priority Date: 11/18/1994
• Status: Expired due to Fees

• Current Assignee: Actew Distribution Ltd., Jemena Gas Networks (NSW) Ltd. (State Grid Corporation of China)
• Original Assignee: Actew Corporation Limited
• Inventors: Barnett, Kenneth Edward
• Primary Examiner(s): Upton, Christopher
• Application Number:
  US08/836,605
• Time in Patent Office: 875 Days
• Field of Search: 210/603, 210/605, 210/608, 210/617, 210/620, 210/621, 210/622, 210/630, 210/150, 210/151, 210/195.1, 210/195.3, 210/202, 210/221.2, 210/258, 210/259, 210/903
• US Class Current: 210/603
• CPC Class Codes: B03D 1/1431 Dissolved air flotation machines
• CPC Class Codes: B03D 1/24 Pneumatic mixing gases or vapours with liquids B01F23/20
• CPC Class Codes: C02F 1/24 by flotation C02F1/465 takes precedence
• CPC Class Codes: C02F 3/085 Fluidized beds
• CPC Class Codes: C02F 3/26 using pure oxygen or oxygen-rich gas
• CPC Class Codes: C02F 3/30 Aerobic and anaerobic processes
• CPC Class Codes: C02F 3/302 Nitrification and denitrification treatment C02F3/308 takes precedence
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage
• CPC Class Codes: Y10S 210/903 Nitrogenous

Abstract

A method of treating wastewater including: biologically treating wastewater under pressure; then reducing the pressure and substantially removing solids by dissolved gas flotation at the reduced pressure.

Claims

1. A method of nitrifying and denitrifying wastewater under pressure comprising:

a. directing wastewater into a pressurized aerobic zone and biologically nitrifying the wastewater under pressure so as to convert ammonia to soluble oxidized nitrogen;

b. transferring at least a portion of the nitrified wastewater from the pressurized aerobic zone to a pressurized deoxygenation zone;

c. deoxidizing the wastewater under pressure within the pressurized deoxygenation zone so as to substantially remove dissolved oxygen from the wastewater;

d. transferring the deoxidized wastewater from the pressurized deoxygenation zone to a pressurized anoxic zone; and

e. biologically denitrifying the wastewater in the anoxic zone under pressure by biologically converting the soluble oxidized nitrogen contained in the wastewater to gaseous nitrogen.

2. The method of claim 1 wherein the pressurized treatment of wastewater in the deoxygenation, anoxic and aerobic zones includes passing the wastewater through a fluidized bed contained within the respective pressurized zones.

3. The method of claim 1 including maintaining the pressure within each of the zones at a pressure of at least 100 kPa.

4. The method of claim 1 including maintaining the pressure within selected zones of the process at pressures of at least 25 kPa.

5. The method of claim 1 including heating the wastewater at a selected point in the treatment process.

6. The method of claim 5 including heating the wastewater prior to the wastewater entering the pressurized deoxidation zone.

7. The method of claim 1 including reducing the dissolved oxygen in the wastewater to effectively zero in the pressurized deoxygenation zone.

8. The method of claim 1 including directing at least a portion of the nitrified wastewater from the pressurized aerobic zone to a pressurized solids separation zone and therein subjecting the wastewater to a pressure less than the pressure present in the nitrification zone.

9. The method of claim 8 including driving an associated tertiary process by subjecting the wastewater to a pressure that is less than the pressure experienced in the solids separation zone.

10. The method of claim 8 including mixing a chemical composition with the wastewater for removing phosphorus at a point downstream from the pressurized nitrification zone.

11. The method of claim 1 including driving an associated tertiary process by subjecting the wastewater to a pressure that is less than the pressure experienced in the nitrification and denitrification phase of the wastewater treatment process.

12. The method of claim 1 including driving an associated filtration and/or disinfection process by subjecting the wastewater to a pressure that is less than the pressure experienced in the nitrification and denitrification phase of the wastewater treatment process.

13. The method of claim 1 including directing an oxygen containing gas into the pressurized nitrification zone and aerating the wastewater under pressure with the oxygen containing gas.

14. A method of nitrifying and denitrifying wastewater under pressure comprising:

a. directing an ammonia containing stream of wastewater into a secondary treatment area;

b. directing the wastewater into a pressurized nitrification reactor and maintaining the wastewater therein under pressure while aerating the wastewater and biologically converting ammonia to nitrate and/or nitrite; and

c. directing the wastewater containing nitrate and/or nitrite to a pressurized denitrification reactor and maintaining the wastewater under pressure and anoxic conditions therein while biologically converting the nitrate and/or nitrite to a gaseous nitrogen.

15. The method of claim 14 including maintaining the pressure within the pressurized aerobic and anoxic reactors at a pressure level of at least 25 kPa and above.

16. The method of claim 14 including maintaining the pressure within the pressurized aerobic and anoxic reactors at a pressure level of at least approximately 200 kPa and above.

17. The method of claim 16 including maintaining the pressure within the pressurized anoxic and aerobic reactors at a level of approximately 500 kPa.

18. The method of claim 16 including directing the wastewater through a fluidized bed in each of the pressurized reactors during the nitrification and denitrification process.

19. The method of claim 14 including directing the denitrified wastewater to a clarification unit housed within a chamber that is maintained at a pressure below the pressure level within the anoxic and aerobic reactors.

20. A pressurized biological wastewater treatment plant for nitrifying and denitrifying wastewater comprising:

a. a pressurized deoxidation reactor for receiving wastewater influent and reducing the dissolved oxygen concentration within the wastewater;

b. a pressurized anoxic reactor located downstream from the pressurized deoxidation reactor for receiving wastewater from the deoxidation reactor and biologically denitrifying the wastewater under pressure such that soluble oxidized nitrogen in the form of nitrates and/or nitrites are converted to gaseous nitrogen;

c. a pressurized aerobic reactor located downstream from the pressurized anoxic reactor for biologically nitrifying wastewater under pressure such that ammonia contained within the wastewater is converted to soluble oxidized nitrogen in the form of nitrates and/or nitrites; and

d. a return line leading from the pressurized nitrification reactor for routing a selected amount of nitrified wastewater to the deoxidation reactor.

21. The pressurized wastewater plant of claim 20 further including a clarifying unit for receiving treated wastewater from at least one of the reactors and subjecting the treated wastewater to a reduction in pressure relative to the pressure experienced in the nitrification and denitrification reactors.

22. The pressurized wastewater treatment plant of claim 21 wherein the clarifying unit is at least partially contained in a surge tank.

23. The pressurized wastewater treatment plant of claim 20 including means for injecting an oxygen containing gas into the pressurized aerobic zone.

24. The pressurized wastewater treatment plant of claim 20 wherein at least one of the pressurized reactors includes a fluid bed through which the wastewater passes.

25. The pressurized wastewater plant of claim 20 wherein the pressurized anoxic and aerobic reactor are pressurized to a pressure level of at least approximately 25 kpa.

26. The pressurized nitrification-denitrification wastewater treatment plant of claim 20 wherein the pressurized anoxic and aerobic reactors are pressurized to a pressure level of at least 200 kpa.