Multivalent metal ion management for low sludge processes
View Patent ↗A method for managing multivalent metal ion concentrations in low-yield wastewater treatment processes. The method includes combining wastewater containing BOD with bacteria-laden sludge in a mainstream reactor to form a mixed liquor, separating the mixed liquor into a clear effluent and an activated sludge stream, returning a first portion of the activated sludge stream to the mainstream reactor, processing a second portion of the activated sludge stream in a sidestream bioreactor, returning at least a portion of the activated sludge stream in the sidestream bioreactor to the mainstream reactor, and adding multivalent metal ions to at least one of the wastewater, the mixed liquor, the activated sludge stream and combinations thereof to reduce the generation of waste activated sludge.
1. A method for reducing waste activated sludge in a wastewater treatment system, the method comprising:
combining wastewater comprising BOD with bacteria-laden sludge in a mainstream reactor to form a mixed liquor;
separating the mixed liquor into a clear effluent and an activated sludge stream;
returning a first portion of the activated sludge stream to the mainstream reactor;
processing a second portion of the activated sludge stream in a sidestream bioreactor;
returning at least a portion of the processed activated sludge stream in the sidestream bioreactor to the mainstream reactor; and
managing multivalent cation content of at least one of the wastewater, the mixed liquor, the activated sludge stream and combinations thereof to reduce the generation of waste activated sludge.
2. The method of claim 1 , wherein managing multivalent cation content of at least one of the wastewater, the mixed liquor, the activated sludge stream and combinations thereof produces a ratio of multivalent metal ions to BOD of about 1:400 (wt/wt) to about 1:25 (wt/wt).
3. The method of claim 1 , wherein managing multivalent cation content of at least one of the wastewater, the mixed liquor, the activated sludge stream and combinations thereof produces a ratio of multivalent metal ions to BOD of about 1:300 (wt/wt) to about 1:50 (wt/wt).
4. The method of claim 1 , wherein managing multivalent cation content of at least one of the wastewater, the mixed liquor, the activated sludge stream and combinations thereof produces a ratio of multivalent metal ions to BOD of about 1:100 (wt/wt) to about 1:50 (wt/wt).
5. The method of claim 1 , wherein multivalent metal ions comprising Fe 3+ are added to at least one of the wastewater, the mixed liquor, the activated sludge stream and combinations thereof.
6. The method of claim 5 , wherein at least one of the mainstream reactor, the sidestream bioreactor and a combination thereof comprises an anaerobic environment.
7. The method of claim 1 , wherein multivalent metal ions comprising at least one of Ca 2+ and Mg 2+ are added to at least one of the wastewater, the mixed liquor, the activated sludge stream and combinations thereof.
8. The method of claim 7 , wherein at least one of the mainstream reactor, the sidestream bioreactor and a combination thereof comprises an aerobic environment.
9. The method of claim 1 , wherein multivalent metal ions are added to the wastewater upstream of the mainstream reactor.
10. The method of claim 1 , wherein multivalent metal ions are added to the mixed liquor prior to separation into a clear effluent and activated sludge stream.
11. The method of claim 1 , wherein multivalent metal ions are added to the activated sludge stream upstream of the sidestream bioreactor.
12. The method of claim 1 , wherein multivalent metal ions are added to the activated sludge stream downstream of the sidestream bioreactor.
13. The method of claim 1 , wherein the sidestream bioreactor is a membrane bioreactor.
14. The method of claim 1 , further comprising passing at least a portion of the activated sludge stream in the sidestream bioreactor through a thickening device before returning the activated sludge stream to the mainstream reactor.
15. The method of claim 1 , further comprising passing the first portion of the activated sludge stream through a screening device before returning the first portion of the activated sludge stream to the mainstream reactor.
16. The method of claim 1 , wherein the method is at least one of a batch process, a continuous process and a combination thereof.
17. A method for reducing waste activated sludge in a wastewater treatment system, the method comprising:
combining wastewater comprising BOD and phosphorus with bacteria-laden sludge in a mainstream reactor to form a mixed liquor;
separating the mixed liquor into a clear effluent and an activated sludge stream;
returning a first portion of the activated sludge stream to the mainstream reactor;
processing a second portion of the activated sludge stream in a sidestream bioreactor;
removing phosphorus from at least a portion of the activated sludge stream processed in the sidestream bioreactor;
transferring at least a portion of the activated sludge stream from which phosphorus has been removed to the mainstream reactor; and
adding multivalent metal ions to at least one of the wastewater, the mixed liquor, the activated sludge stream and combinations thereof to reduce the generation of waste activated sludge.
18. The method of claim 17 , wherein adding multivalent metal ions to at least one of the wastewater, the mixed liquor, the activated sludge stream and combinations thereof produces a ratio of multivalent metal ions to BOD of about 1:400 (wt/wt) to about 1:25 (wt/wt).
19. The method of claim 17 , wherein adding multivalent metal ions to at least one of the wastewater, the mixed liquor, the activated sludge stream and combinations thereof produces a ratio of multivalent metal ions to BOD of about 1:300 (wt/wt) to about 1:50 (wt/wt).
20. The method of claim 17 , wherein adding multivalent metal ions to at least one of the wastewater, the mixed liquor, the activated sludge stream and combinations thereof produces a ratio of multivalent metal ions to BOD of about 1:100 (wt/wt) to about 1:50 (wt/wt).
21. The method of claim 17 , wherein the multivalent metal ions comprise Fe 3+ .
22. The method of claim 21 , wherein at least one of the mainstream reactor, the sidestream bioreactor and a combination thereof comprises an anaerobic environment.
23. The method of claim 22 , wherein the multivalent metal ions comprise at least one of Ca 2+ , Mg 2+ and a combination thereof.
24. The method of claim 17 , wherein at least one of the mainstream reactor, the sidestream bioreactor and a combination thereof comprises an aerobic environment.
25. The method of claim 17 , wherein the multivalent metal ions are added to the wastewater upstream of the mainstream reactor.
26. The method of claim 17 , wherein the multivalent metal ions are added to the mixed liquor prior to separation into a clear effluent and activated sludge stream.
27. The method of claim 17 , wherein the multivalent metal ions are added to the activated sludge stream upstream of the sidestream bioreactor.
28. The method of claim 17 , wherein the multivalent metal ions are added to the activated sludge stream downstream of the sidestream bioreactor.
29. The method of claim 17 , wherein the sidestream bioreactor is a membrane bioreactor.
30. The method of claim 17 , further comprising passing at least a portion of the activated sludge in the sidestream bioreactor through a thickening device before returning the activated sludge to the mainstream reactor.
31. The method of claim 17 , further comprising passing the first portion of activated sludge through a screening device before returning the first portion of the activated sludge to the mainstream reactor.
32. The method of claim 17 , wherein the method is at least one of a batch process, a continuous process and a combination thereof.
33. The method of claim 17 , wherein removing phosphorus from the second portion of the activated sludge comprises adding a source of multivalent metal ions to the activated sludge to precipitate phosphate solids and separating and removing the phosphate solids from the activated sludge.
34. A method for reducing waste activated sludge in a wastewater treatment system, the method comprising:
combining wastewater comprising BOD and phosphorus with bacteria-laden sludge in a mainstream reactor to form a mixed liquor;
separating the mixed liquor into a clear effluent and activated sludge stream;
returning a first portion of the activated sludge stream to the mainstream reactor;
processing a second portion of the activated sludge stream in a sidestream bioreactor;
returning at least a portion of the processed activated sludge stream to the mainstream reactor; and
adding Fe 3+ ions to at least one of the wastewater, the mixed liquor, the activated sludge stream and combinations thereof to reduce the generation of waste activated sludge,
wherein at least one of the mainstream reactor, the sidestream bioreactor and a combination thereof comprises an anaerobic environment.
35. The method of claim 34 , wherein adding Fe 3+ ions to at least one of the wastewater, the mixed liquor, the activated sludge stream and combinations thereof produces a ratio of multivalent metal ions to BOD of about 1:400 (wt/wt) to about 1:25 (wt/wt).
36. The method of claim 34 , wherein adding Fe 3+ ions to at least one of the wastewater, the mixed liquor, the activated sludge stream and combinations thereof produces a ratio of multivalent metal ions to BOD of about 1:300 (wt/wt) to about 1:50 (wt/wt).
37. The method of claim 34 , wherein adding Fe 3+ ions to at least one of the wastewater, the mixed liquor, the activated sludge stream and combinations thereof produces a ratio of multivalent metal ions to BOD of about 1:100 (wt/wt) to about 1:50 (wt/wt).
38. The method of claim 34 , wherein the Fe 3+ ions are added to the influent upstream of the mainstream reactor.
39. The method of claim 34 , wherein the Fe 3+ ions are added to the activated sludge stream upstream of the sidestream bioreactor.
40. The method of claim 34 , wherein the sidestream bioreactor is a membrane bioreactor.
41. The method of claim 34 , further comprising passing at least a portion of the activated sludge stream in the sidestream bioreactor through a thickening device before returning the activated sludge stream to the mainstream bioreactor.
42. The method of claim 34 , wherein the method is at least one of a batch process, a continuous process and a combination thereof.
43. The method of claim 34 , further comprising removing phosphorus from at least a portion of the activated sludge stream processed in the sidestream bioreactor before returning the activated sludge stream to the mainstream reactor.
44. The method of claim 34 , further comprising adding at least one of Ca 2+ , Mg 2+ and a combination thereof, wherein at least one of the mainstream reactor, the sidestream bioreactor and combination thereof comprises an aerobic environment.
45. The method of claim 1 , wherein managing multivalent cation content comprises promoting formation of a biopolymer fraction in at least one of the wastewater, the mixed liquor, the activated sludge stream and combinations thereof.
46. The method of claim 45 , wherein the biopolymer fraction comprises a divalent cation-bound biopolymer.
47. The method of claim 46 , wherein promoting formation of the divalent cation-bound biopolymer comprises supplying at least one of Ca 2+ and Mg 2+ .
48. The method of claim 45 , wherein the biopolymer fraction comprises an Fe-associated biopolymer.
49. The method of claim 48 , wherein promoting formation of the Fe-associated biopolymer comprises increasing floc Fe content.
50. The method of claim 1 , wherein managing multivalent cation content comprises associating organic matter in at least one of the wastewater, the mixed liquor, the activated sludge stream and combinations thereof with multivalent cations.
51. The method of claim 50 , wherein the multivalent cations comprise divalent cations.
52. The method of claim 51 , wherein the divalent cations comprise at least one of Ca 2+ and Mg 2+ .
53. The method of claim 50 , wherein the multivalent cations comprise Fe 3+ ions.
54. The method of claim 1 , further comprising removing phosphorus from at least a portion of the processed activated sludge stream.
55. The method of claim 44 , wherein adding Fe 3+ ions comprises promoting formation of an Fe-associated biopolymer in at least one of the wastewater, the mixed liquor, the activated sludge stream and combinations thereof.