Process for the treatment of sludge

Patent metadata

Field	Value
Publication number	US-11198632-B2
Application number	US-201816496050-A
Country	US
Kind code	B2
Filing date	Mar 29, 2018
Priority date	Mar 30, 2017
Publication date	Dec 14, 2021
Grant date	Dec 14, 2021

Abstract

A method for treating a sludge derived from sewage or wastewater, the method comprising subjecting the sludge to a treatment step at a pH of 8.9 or greater and a free ammonia (FA) content of 100 mg NH 3 —N/L or greater. The treated sludge may be fed to a bioreactor to produce methane.

First claim

The invention claimed is:

1. A method for treating a sludge derived from sewage or wastewater, the method comprising:
a) subjecting the sludge to a treatment step at a pH of 8.9 or greater and a free ammonia content of 100 mg NH 3 —N/L or greater;
b) sending the sludge from step (a) to an anaerobic digester, to form methane and an anaerobic digestion liquor in the anaerobic digester; and
c) returning at least part of the anaerobic digestion liquor to step (a),
wherein treatment of the sludge with free ammonia at a pH of 8.9 or greater in step (a) is on an intermittent basis, and wherein the sludge is treated with free ammonia at a pH of 8.9 or greater for a period of from 2 hours to 7 days, followed by a non-treatment period of from 1 day to 3 months.

2. A method as claimed in claim 1 wherein the sludge comprises a secondary sludge from a secondary settler or from a bioreactor for treating sewage or wastewater, or the sludge comprises a primary sludge from a sewage or wastewater treatment plant, or the sludge comprises a primary sludge collected from a primary settler or a sludge collected from a screen.

3. A method as claimed in claim 1 wherein the pH in step (a) is from 8.9 to 10.5, or from 8.9 to 10.0, or from 8.9 to 9.5, or from 9.0 to 9.5, or from 9.1 to 9.5, or from 9.2 to 9.5, or from 9.3 to 9.5, or about 9.3.

4. A method as claimed in claim 1 wherein the free ammonia concentration in step (a) ranges from 100 to 1000 mg NH 3 —N/L, or from 250 to 1000 mg NH 3 —N/L, or from 250 to 900 mg NH 3 —N/L, or from 250 to 800 mg NH 3 —N/L, or from 250 to 700 mg NH 3 —N/L, or from 250 to 680 mg NH 3 —N/L, or from 400 to 700 mg NH 3 —N/L, or from 420 to 680 mg NH 3 —N/L.

5. A method as claimed in claim 1 wherein the pH is controlled to fall within the range of 8.9 or greater and the pH is controlled by monitoring the pH and adding an alkaline agent if the pH drops below 8.9.

6. A method as claimed in claim 1 wherein the free ammonia content in step (a) is obtained by adding a liquid containing dissolved ammonium (NH 4 + ) having a concentration such that at the pH of step (a), the free ammonia content is achieved in the reactor in which step (a) is conducted.

7. A method as claimed in claim 6 wherein the liquid containing dissolved ammonium has a dissolved ammonium concentration of from 0.5 to 4 g/L NH 4 + —N, or from 1.0 to 3.0 g/L NH 4 + —N, or from 1.0 to 2.0 g/L NH 4 + —N.

8. A method as claimed in claim 1 wherein the sludge has a residence time in step (a) of from 2 hours to 1 week, or from 4 hours to 48 hours, or from 6 hours to 24 hours.

9. A method as claimed in claim 1 wherein the sludge is being fed to a downstream reactor in step (b) where methane is being produced and treatment of the sludge with free ammonia occurs on a continuous basis.

10. A method as claimed in claim 9 wherein anaerobic liquor is fed continuously to a reactor and alkali addition occurs when the pH drops below 8.9.

11. A method as claimed in claim 1 wherein the sludge is treated with free ammonia at a pH of 8.9 or greater for a period of from 2 hours to 7 days, followed by a non-treatment period of from 1 day to 1 month, or from 7 days to 1 month.

12. A method as claimed in claim 1 wherein the method comprises obtaining a primary sludge from sewage or wastewater, treating the primary sludge at a pH of 8.9 or greater and a free ammonia content of 100 mg NH 3 —N/L or greater to form a treated sludge, feeding the treated sludge to an anaerobic digester to form methane and an anaerobic digestion liquor and returning at least some of the anaerobic digestion liquor to the primary sludge treatment step.

13. A method as claimed in claim 12 wherein a primary settler forms a sludge stream and a liquid stream, the liquid stream being fed to a bioreactor to form a secondary sludge, the secondary sludge also being fed to the anaerobic digester.

14. A method for treating a sludge derived from sewage or wastewater, the method comprising
feeding a wastewater or sewage to a bioreactor, obtaining a secondary sludge from the bioreactor, treating the secondary sludge at a pH of 8.9 or greater and a free ammonia (FA) content of 100 mg NH 3 —N/L or greater to obtain a treated secondary sludge, feeding the treated secondary sludge to an anaerobic digester to form methane and an anaerobic digestion liquor and passing at least some of the anaerobic digestion liquor to the step of treating the secondary sludge.

15. A method as claimed in claim 14 wherein the secondary sludge is thickened prior to the step of treating the secondary sludge with free ammonia.

16. A method as claimed in claim 15 wherein the sludge is thickened to a solids level in the range of from 2% to 15% by weight, or from 4% to 8% by weight.

17. A method for treating wastewater comprising the steps of treating wastewater or wastewater sludge in a bioreactor, passing part of a secondary sludge generated in the bioreactor to an anaerobic digester, treating another part of the secondary sludge produced in the bioreactor at a pH of 8.9 or greater and a free ammonia (FA) content of 100 mg NH 3 —N/L or greater, and forwarding treated sludge to the bioreactor, wherein an anaerobic digestion liquor is removed from the anaerobic digester and part of the anaerobic digestion liquor is passed to the free ammonia treatment step.

18. A method as claimed in claim 17 wherein some of the anaerobic digestion liquor is returned to the bioreactor.

Assignees

• Univ Queensland

Inventors

• Wang Qilin
• Yuan Zhiguo
• Duan Haoran
• Wei Wei

Classifications

• C02F2209/06

  pH · CPC title

• C02F11/04 Primary

  Anaerobic treatment; Production of methane by such processes · CPC title

• C02F2209/14

  NH3-N · CPC title

• C02F1/66

  by neutralisation; pH adjustment (for degassing C02F1/20; using ion-exchange C02F1/42; for flocculation or precipitation of suspended impurities C02F1/52; for removing dissolved compounds C02F1/58) · CPC title

• Y02E50/30

  Fuel from waste, e.g. synthetic alcohol or diesel · CPC title