Methods and apparatus for treating wastewater employing a high rate clarifier and a membrane

• US 7,410,584 B2
• Filed: 10/08/2007
• Issued: 08/12/2008
• Est. Priority Date: 01/31/2005
• Status: Expired due to Fees

• Current Assignee: Alfa Laval, Inc. (Canada) (ALFA Laval AB)
• Original Assignee: Ashbrook Simon-Hartley Operations, LP
• Inventors: Devine, Jeffrey S.
• Primary Examiner(s): PRINCE JR, FREDDIE GARY
• Application Number:
  US11/868,811
• Publication Number:
  US 20080116130A1
• Time in Patent Office: 309 Days
• Field of Search: 210/606, 210/614, 210/620, 210/621, 210/623, 210/630, 210/252, 210/259, 210/513, 210/532.1, 210/903, 210/906
• US Class Current: 210/605
• CPC Class Codes: B01D 2311/04 Specific process operations in the feed stream; Feed pretreatment
• CPC Class Codes: B01D 2311/12 Addition of chemical agents
• CPC Class Codes: B01D 61/145 Ultrafiltration
• CPC Class Codes: B01D 61/147 Microfiltration
• CPC Class Codes: B01D 61/16 Feed pretreatment
• CPC Class Codes: C02F 1/444 by ultrafiltration or microfiltration
• CPC Class Codes: C02F 3/1268 Membrane bioreactor systems
• CPC Class Codes: C02F 3/308 Biological phosphorus removal
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage
• CPC Class Codes: Y10S 210/903 Nitrogenous
• CPC Class Codes: Y10S 210/906 Phosphorus containing

Abstract

Methods and apparatus for treating wastewater are described, one method embodiment including the steps of flowing a stream comprising mixed liquor suspended solids and fixed growth solids to a high rate clarification stage, forming a clarifier effluent, a first waste activated sludge stream, and a return waste activated sludge stream. The high rate clarifier effluent stream then flows to a membrane stage that includes a membrane media, producing a membrane reject (retentate) stream and a treated effluent (permeate) stream. Optionally, the methods include routing a screened raw wastewater to an anaerobic and/or aerated anoxic stage and introducing a gas comprising oxygen to the wastewater during the aerated anoxic stage, and optionally allowing the product of this stage to flow to an aeration stage prior to the high rate clarification stage.

Claims

1. A method of treating wastewater comprising:

a) flowing a stream comprising mixed liquor suspended solids and fixed growth solids to a high rate clarification stage, thus forming a high rate clarifier effluent, a first waste activated sludge stream, and a return activated sludge stream; and

b) flowing the high rate clarifier effluent stream to a membrane stage comprising a membrane media, producing a membrane reject stream and a treated effluent permeate stream.

2. The method of claim 1 comprising, prior to the high rate clarification stage (a), a step (aa) of subjecting a screened raw wastewater to one or more steps selected from the group consisting of (i) an aerated anoxic stage and introducing a gas comprising oxygen to the wastewater during the aerated anoxic stage;

(ii) an anaerobic stage; and

(iii) a mixed only anoxic stage, to provide a level of nitrification and denitrification resulting in substantial nitrogen removal, and a level of biological or chemical phosphorus removal.

3. The method of claim 2 comprising allowing the product of step (aa) to flow to a stage selected from the group consisting of an aeration stage and a post anoxic stage prior to flowing to the high rate clarification stage, said product comprising mixed liquor suspended solids and fixed growth solids in which carbonaceous biochemical oxygen demand (CBOD) is consumed along with reduced nitrogen which is nitrified and denitrified.

4. The method of claim 2 wherein a portion of the first waste activated sludge stream is returned to the aerated anoxic stage as return activated sludge (RAS).

5. The method of claim 2 wherein a portion of the stream comprising mixed liquor suspended solids and fixed growth solids is returned to the aerated anoxic stage as mixed liquor suspended solids/fixed growth solids recycle.

6. The method of claim 1 wherein a portion of the membrane reject stream is recycled to a point in the process upstream of the high rate clarifier.

7. The method of claim 6 wherein a portion of the membrane reject stream is routed to waste activated sludge storage.

8. The method of claim 1 wherein the membrane is selected from the group consisting of hollow fiber membranes, flat sheet membranes, rolled sheet membranes, tubular membranes, spiral wound membranes, vortex devices, pleated sheet membranes, tube ribbon membranes, and combinations thereof.

9. The method of claim 1 comprising admitting a gas comprising oxygen as a membrane scouring agent.

10. The method of claim 1 comprising using a gas comprising oxygen to flush scum and waste activated sludge from the membrane.

11. The method of claim 1 wherein the membrane media is submerged at a reasonable depth in the high rate clarifier effluent to enhance oxygen transfer to the membrane reject stream and reduce or eliminate suction pressure required to withdraw the treated effluent permeate stream through the membrane media.

12. An apparatus for treating wastewater comprising:

a) a high rate clarifier adapted to accept a stream comprising mixed liquor suspended solids and fixed growth solids, and form a high rate clarifier effluent, a first waste activated sludge stream, and a return activated sludge stream; and

b) a membrane unit comprising a membrane media, the membrane unit adapted to accept the high rate clarifier effluent, and produce a membrane reject stream and a treated effluent permeate stream.

13. The apparatus of claim 12 comprising an aerated anoxic vessel fluidly connected to and upstream of the high rate clarifier.

14. The apparatus of claim 13 comprising means for introducing a gas comprising oxygen to the wastewater adapted to traverse through the aerated anoxic vessel sufficient for mixing and partial oxygenation of the wastewater for producing an acceptable level of simultaneous nitrification and denitrification.

15. The apparatus of claim 12 comprising means for allowing the product of step (a) to flow to an aeration vessel, producing the stream comprising mixed liquor suspended solids and fixed growth solids.

16. The apparatus of claim 15 comprising means for flowing the stream comprising mixed liquor suspended solids and fixed growth solids from the aeration vessel to the high rate clarifier.

17. The apparatus of claim 12 wherein the high rate clarifier has a surface overflow rate that is greater than 500 gallons/day/ft² at average design influent flow rate.

18. The apparatus of claim 12 wherein the high rate clarifier has a surface overflow rate that is greater than 2,000 gallons/day/ft² at average design influent flow rate.

19. The apparatus of claim 12 wherein the high rate clarifier has a surface overflow rate that ranges from about 500 to about 2,000 gallons/day/ft² at design average flow rates and hydraulic residence times less than about 2 hours.

20. The apparatus of claim 12 wherein the high rate clarifier comprises a settler selected from plate settlers and tube settlers.

21. The apparatus of claim 12 wherein the high rate clarifier is part of a package wastewater treatment plant including an aerated anoxic vessel and an aeration vessel.

22. The apparatus of claim 12 comprising a hydraulics optimization baffle in the high rate clarifier.

23. The apparatus of claim 12, the membrane unit comprising a level switch that controls treated effluent flow from the membrane unit and backflushing of the membrane media.

24. The apparatus of claim 12 comprising means for introducing a gas comprising oxygen as a membrane media scouring agent and membrane unit oxygenation system for continuous biological treatment.

25. The apparatus of claim 12 wherein the membrane media is submerged at a reasonable depth in the high rate clarifier effluent to enhance oxygen transfer to the membrane reject stream and reduce or eliminate suction pressure required to withdraw the treated effluent permeate stream through the membrane media.