Wastewater treatment system with membrane separators and provision for storm flow conditions

• US 7,147,777 B1
• Filed: 05/09/2005
• Issued: 12/12/2006
• Est. Priority Date: 05/09/2005
• Status: Active Grant

• Current Assignee: Ovivo Inc. (Susanne Klatten, MBA)
• Original Assignee: Eimco Water Technologies, LLC
• Inventors: Porteous, James
• Primary Examiner(s): Prince, Fred G.
• Application Number:
  US11/125,595
• Time in Patent Office: 582 Days
• Field of Search: 210/605, 210/620, 210/621, 210/622, 210/623, 210/630, 210/194, 210/195.2, 210/252, 210/259
• US Class Current: 210/605
• CPC Class Codes: C02F 3/1268 Membrane bioreactor systems
• 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

Abstract

In a wastewater treatment system and process utilizing membrane bioreactors (MBRs), multiple, parallel series of tanks or stages each include, an MBR stage. Under conditions of normal flow volume into the system, influent passes through several parallel series of stages or process lines, which might be, for example, an anoxic stage, an aeration stage and an MBR stage. From the MBR stages a portion of M.L.S.S. is cycled through one or more thickening MBRs of similar process lines, for further thickening and further processing and digesting of the sludge, while a majority portion of the M.L.S.S. is recycled back into the main process lines. During peak flow conditions, such as storm conditions in a combined storm water/wastewater system, all of the series of stages with their thickening MBRs are operated in parallel to accept the peak flow, which is more than twice normal flow. M.L.S.S. is recycled from all MBR stages to the upstream end of each of all the parallel process lines, mixing with influent wastewater, and the last one or several process lines no longer act to digest the sludge. Another advantage is that with the thickened sludge in the last process line of basins, which ordinally act to digest the sludge, there is always sufficient biomass in the system to handle peak flow, the biomass being available if needed for a sudden heavy flow or an event that might bring a toxic condition into the main basins.

Claims

1. A sewage treatment system with a series of parallel main process lines including anoxic and aerobic zones and an MBR zone in series, with inflow means for receiving influent wastewater into the main process lines, and at least one additional, special process line having similar zones but being normally operated to receive a portion of M.L.S.S. from the main process lines, the special process line having means for internal recycling of sludge among the zones during normal operation, so as to produce a further thickened and stabilized or digested W.A.S. to be removed from the special process line during normal operation, and including means for recycling a majority of M.L.S.S. exiting the main process lines to re-enter the main process lines to mix with wastewater in the main process lines, whereby the system can be operated in a second, surge or storm mode of operation at more than twice normal design flow, wherein all process lines are operated in the same manner, with parallel streams of wastewater being processed serially through the anoxic, aeration and MBR zones, thereby maintaining equilibrium in the system by removing water via the MBRs at a rate equal to influent wastewater flow, without the need to remove W.A.S. during a period of such surge or storm mode.

2. The sewage treatment system of claim 1, wherein the MBRs are sized for a design flow through said main process lines of Q, and wherein the system in a surge or storm mode of operation is capable of receiving influent greater than 2Q.

3. The sewage treatment system of claim 2, wherein the system in the surge or storm mode of operation is capable of receiving influent of at least about 3Q.

4. The sewage treatment system of claim 1, wherein the means for recycling M.L.S.S. from the main process lines recycles at a rate of about 1Q to 10Q, where Q is the flow rate of influent wastewater into the system.

5. The sewage treatment system of claim 4, wherein the means for recycling operates at a rate of about 4Q.

6. The sewage treatment system of claim 1, wherein the MBR zones in all process lines are positioned as the last zone in the series of zones.

7. The sewage treatment system of claim 1, wherein the portion of M.L.S.S. received in the special process line is received directly in the MBR zone of the special process line.

8. The sewage treatment system of claim 1, wherein the stabilized or digested W.A.S. removed from the MBR zone of the special process line is at about 1% to 5% solids content.

9. The sewage treatment system of claim 8, wherein the stabilized or digested W.A.S. removed from the MBR zone of the special process line is at about 3% solids content.

10. The sewage treatment system of claim 1, wherein the inflow means provides for influent wastewater to enter into the anoxic zones.

11. The sewage treatment system of claim 1, wherein each process line further includes an anaerobic zone, upstream of the anoxic zone, and wherein influent enters the main process lines at the anaerobic zones, via the inflow means.

12. The sewage treatment system of claim 11, wherein each process line comprises zones as follows:

anaerobic, anoxic, aerobic, anoxic, MBR.

13. The sewage treatment system of claim 1, wherein the aerobic zones of each process line are controlled to allow simultaneous nitrification/denitrification wherein dissolved oxygen content is controlled to effect nitrification and denitrification in the same zone.

14. A method for operating a sewage treatment system, the system including a series of parallel main process lines each including anoxic and aerobic zones and an MBR zone in series, with influent wastewater received in the main process lines, and at least one additional, special process line having similar zones, comprising the steps of:

in the normal operation mode in which influent wastewater is approximately at design flow, normally operating the system to deliver a portion of M.L.S.S. from the main process lines to the special process lines, and internally recycling sludge among the zones of the special process line during normal operation, so as to produce a further thickened and stabilized or digested W.A.S.,

in the normal operation mode, removing stabilized or digested W.A.S. from the MBR zone of the special process line,

in the normal operation mode, recycling effluent M.L.S.S. from the main process lines back to re-enter the main process lines to mix with wastewater in the main process lines while delivering said portion of M.L.S.S. to the special process line wherein further thickening and digestion or stabilization of sludge occur, and

in a surge or storm mode of operation when influent wastewater flow rate is more than twice design flow, receiving the influent wastewater in all process lines and operating all process lines in the same manner, with parallel streams of influent wastewater being processed serially through the anoxic, aeration and MBR zones similarly and in parallel through all process lines including the special process line, and

in the surge or storm mode of operation, recycling effluent M.L.S.S. from all process lines back to enter the process lines to mix with wastewater in the process lines,

thereby, in the surge or storm mode, maintaining equilibrium in the system by removing water via the MBRs of all process lines at a rate essentially equal to influent wastewater flow, without the need to remove W.A.S. during such surge or storm mode.

15. The method of claim 14, including a step of transitioning between the normal mode of operation and the surge or storm mode of operation, the transitioning step including discontinuing delivery of M.L.S.S. from the main process lines to the special process line, discontinuing internal recycling in the special process line, introducing influent and recycled wastewater in the manner of the main process lines to the special process line, discontinuing removal of stabilized or digested W.A.S. from the special process line, recycling M.L.S.S. from all process lines to re-enter all process lines to mix with wastewater in the process lines, and redistributing solids from the special process line to all process lines.

16. The method of claim 14, wherein, with W.A.S. not being removed from the special process line during the surge or storm mode, solids are held in the system during the surge or storm rate of inflow and are allowed to increase from about 0.8% or 1% solids up to about 1.8% solids or more, until the storm or surge event passes.

17. The method of claim 16, wherein, after the surge or storm event passes, the special process line is converted back to normal mode of operation, digesting or stabilizing sludge, receiving sludge from the normal process lines, further thickening sludge and with stabilized and thickened sludge removed from the special process line.

18. The method of claim 14, wherein in normal operation M.L.S.S. exits the main process lines at approximately 1% solids, and wherein thickened and stabilized or digested sludge is wasted from the special process line at approximately 3% solids;

and wherein, in surge or storm mode of operation, M.L.S.S. is continuously recycled through all process lines thus gradually increasing solids content of the M.L.S.S. during the surge or storm event.

19. The method of claim 14, wherein the process lines each include an anaerobic zone upstream of the anoxic zone, with influent wastewater in the main process lines being delivered to the anaerobic zones, and with M.L.S.S. being recycled so as to bypass the anaerobic zones.

20. The method of claim 14, wherein the aerobic zone of each process line comprises a simultaneous nitrification/denitrification zone wherein dissolved oxygen content is controlled to effect nitrification and denitrification in the same zone.

21. The method of claim 14, wherein, in the surge or storm mode of operation, W.A.S. is not removed unless and until solids content in the system reaches about 1.8%, after which wasting occurs from all process lines.