Simultaneous anoxic biological phosphorus and nitrogen removal with energy recovery

• US 9,656,893 B2
• Filed: 03/17/2014
• Issued: 05/23/2017
• Est. Priority Date: 09/20/2010
• Status: Active Grant

• Current Assignee: American Water Works Company Incorporated
• Original Assignee: American Water Works Company Incorporated
• Inventors: Giraldo, Eugenio William
• Primary Examiner(s): Prince, Fred
• Application Number:
  US14/216,052
• Publication Number:
  US 20140197097A1
• Time in Patent Office: 1,163 Days
• Field of Search: 210603, 210605, 210621, 210623, 210630, 210252, 210259, 210903, 210906
• CPC Class Codes: C02F 2303/10 Energy recovery
• CPC Class Codes: C02F 2303/16 Regeneration of sorbents, filters
• CPC Class Codes: C02F 3/1215 Combinations of activated sludge treatment with precipitation, flocculation, coagulation and separation of phosphates
• CPC Class Codes: C02F 3/1268 Membrane bioreactor systems
• CPC Class Codes: C02F 3/1273 Submerged membrane bioreactors
• CPC Class Codes: C02F 3/28 Anaerobic digestion processes
• CPC Class Codes: C02F 3/2846 using upflow anaerobic sludge blanket [UASB] reactors
• CPC Class Codes: C02F 3/302 Nitrification and denitrification treatment C02F3/308 takes precedence
• CPC Class Codes: C02F 3/307 characterised by direct conversion of nitrite to molecular nitrogen, e.g. by using the Anammox process
• CPC Class Codes: C02F 3/308 Biological phosphorus removal
• CPC Class Codes: Y02E 50/30 Fuel from waste, e.g. synthetic alcohol or diesel
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage
• CPC Class Codes: Y02W 10/30 Wastewater or sewage treatment systems using renewable energies

Abstract

Methods and systems are provided for treating wastewater to simultaneously remove nitrogen, carbon, and phosphorus, while recovering energy in the form of methane and carbon dioxide. An ammonia-containing stream is directed to a pretreatment tank that produces excess sludge, biogas, and a pretreated stream. The pretreated stream has at least 45% less carbon than the ammonia-containing stream. The pretreated stream is then directed to an anoxic tank, which promotes phosphorus release and fermentation of particulate and dissolved organic matter. The mixed liquor is transferred to an aerated tank having low dissolved oxygen concentrations to promote development of phosphorus-release bacteria that is eventually recycled to the anoxic tank by way of the return activated sludge. Simultaneous nitrification, denitrification, and phosphorus release occur in the aerated tank. A membrane tank separates treated effluent from activated sludge in a membrane tank.

Claims

1. A process for treating wastewater to simultaneously remove organic matter, nitrogen, and phosphorus with energy recovery, the process comprising:

providing a wastewater stream in a pretreatment tank that produces, at least, excess sludge, biogas, and a pretreated stream, wherein the pretreated stream has 45% to 70% less carbon than the wastewater stream and the biogas comprises at least methane and carbon dioxide;

flowing the pretreated stream and return activated sludge to an anoxic tank operating under anoxic conditions;

mixing the pretreated stream and the return activated sludge in the anoxic tank to form a mixed liquor and to initiate phosphorus release and fermentation of particulate organic matter and dissolved organic matter;

transferring the mixed liquor to an aerated tank operating under microaerophilic conditions, to simultaneously effectuate nitrification, denitrification, phosphorous release, and phosphorus uptake in the aerated tank; and

transferring the mixed liquor to a membrane tank that separates treated effluent from activated sludge containing microorganisms, wherein a first portion of the activated sludge is returned to the anoxic tank as the return activated sludge.

2. The process of claim 1, wherein the wastewater stream is plant influent wastewater that is to be treated by carbon removal.

3. The process of claim 2, wherein the biogas is treated such that it can be used to power a wastewater treatment plant that treats the plant influent wastewater by offsetting energy requirements of the wastewater treatment plant.

4. The process of claim 1, wherein the biogas comprises about 60% of the methane.

5. The process of claim 1, wherein the pretreatment tank is an upflow anaerobic sludge blanket (UASB) reactor.

6. The process of claim 1, wherein the microaerophilic conditions in the aerated tank promote the fermentation of the particulate organic matter in the mixed liquor and allow for development of a microbial population used for phosphorus removal.

7. The process of claim 1, wherein a portion of the wastewater stream bypasses the pretreatment tank and is directed to the anoxic tank.

8. The process of claim 1, wherein the pretreatment tank utilizes a one-stage activated sludge system.

9. The process of claim 1, wherein a second portion of the activated sludge is transferred to the aerated tank operating under microaerophilic conditions.

10. A method for treating a wastewater stream while recovering energy, the method comprising:

providing the wastewater stream in a pretreatment tank that comprises anaerobic microorganisms that react with the wastewater stream by removing carbon to produce biogas and a pretreated stream, wherein the pretreated stream has 45% to 70% less carbon than the wastewater stream and wherein the biogas comprises at least methane and carbon dioxide;

upgrading the biogas produced by removing a majority of the carbon dioxide;

using the upgraded biogas to generate electric power to offset part or all of electric power used at a water treatment plant that is treating the wastewater stream;

flowing the pretreated stream to at least two tanks in series for removal of organic matter, nitrogen, and phosphorus;

in the at least two tanks, separating excess sludge from treated effluent after removal of organic matter, nitrogen, and phosphorus; and

returning the excess sludge to the pretreatment tank for additional carbon removal, wherein biogas produced from the additional carbon removal is upgraded and used to generate additional electric power.

11. The method of claim 10, wherein about 60% of the carbon present in the wastewater stream is removed by a carbon removal pretreatment processes.

12. The method of claim 10, wherein the biogas is comprised of up to 80% methane.

13. The method of claim 10, wherein at least one of the two or more tanks comprises an anoxic tank and wherein phosphorus release occurs in the anoxic tank.

14. The method of claim 10, wherein at least one of the two or more tanks comprises an aerated tank and wherein nitrification, denitrification, phosphorus release, and phosphorus uptake occur simultaneously in the aerated tank.

15. The method of claim 14, wherein a concentration of dissolved oxygen in the aerated tank is less than 1.0 mg/l of fluid.

16. A system for treating wastewater to simultaneously remove organic matter, nitrogen, and phosphorus with energy recovery, the system comprising:

a pretreatment tank that receives plant influent wastewater and that comprises anaerobic microorganisms that react with the plant influent wastewater to produce, at least, biogas comprising methane, excess sludge, and a pretreated stream, the pretreated stream having 45% to 70% less carbon than the plant influent wastewater stream;

an anoxic tank that receives the pretreated stream and return activated sludge and mixes them to form a mixed liquor and to initiate phosphorus release and fermentation of particulate organic matter and dissolved organic matter;

an aerated tank that receives the mixed liquor from the anoxic tank, wherein the aerated tank operates under microaerophilic conditions, to simultaneously effectuate nitrification, denitrification, phosphorous release, and phosphorus uptake in the aerated tank; and

a membrane tank that separates plant effluent wastewater from activated sludge, a portion of the activated sludge being recycled to the anoxic tank as the return activated sludge.

17. The system of claim 16, wherein the aerated tank comprises one or more aerated tanks.

18. The system of claim 16, wherein nitrification, denitrification, phosphorus release, and phosphorus uptake occur simultaneously in the aerated tank.

19. The system of claim 16, wherein the concentration of dissolved oxygen in the anoxic tank is less than 0.3 mg/l of the mixed liquor.