Combination membrane/biolytic filtration

• US 7,708,887 B2
• Filed: 11/08/2006
• Issued: 05/04/2010
• Est. Priority Date: 11/08/2005
• Status: Expired due to Fees

• Current Assignee: Evoqua Water Technologies LLC
• Original Assignee: Siemen Water Technologies Corporation (Siemens AG)
• Inventors: Cameron, Dean Osman, Johnson, Warren Thomas, Biltoft, Bruce Gregory
• Primary Examiner(s): Upton; Christopher
• Application Number:
  US12/092,755
• Publication Number:
  US 20080290025A1
• Time in Patent Office: 1,273 Days
• Field of Search: 210/614, 210/615, 210/617, 210/631, 210/650, 210/741, 210/744, 210/104, 210/106, 210/150, 210/151, 210/257.2, 210/258, 210/259
• US Class Current: 210/614
• CPC Class Codes: C02F 1/44 by dialysis, osmosis or reverse osmosis general membrane separation processes B01D61/00, membrane modules B01D63/00, electrodialysis C02F1/4693, combination of membrane modules and bioreactors C02F3/1268
• CPC Class Codes: C02F 2201/005 Valves
• CPC Class Codes: C02F 2303/16 Regeneration of sorbents, filters
• CPC Class Codes: C02F 3/06 using submerged filters
• CPC Class Codes: C02F 3/1242 Small compact installations for use in homes, apartment blocks, hotels or the like
• CPC Class Codes: C02F 3/1273 Submerged membrane bioreactors
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage

Abstract

Described herein are methods and systems for combination membrane/biolytic filtration. In one embodiment a filtration system is operated under suction. The arrangement includes a feed tan (5) having a smaller filtrate vessel (6) positioned therein. The region within, the feed tank (5) not occupied by the filtrate vessel (6) is partially filled with layers of decomposing and decomposed solid organic waste material to form an aerobic filter bed (7) of the type used in biolytic filtration as described above. A further module vessel (8) is mounted within the filtrate vessel (6) to form a membrane chamber (9) containing a membrane filtration module (10).

Claims

1. A wastewater treatment system comprising:

an aerobic compost bed;

an inlet configured to supply wastewater to said aerobic compost bed;

a membrane filter device including one or more hollow, permeable membranes including walls with feed sides and filtrate sides, the feed sides being in fluid communication with said aerobic compost bed;

a pump coupled to said membrane filter device, said pump being selectively operable to provide a filtration operation by producing a pressure differential across the walls of said membranes to cause flow of feed liquid from the aerobic compost bed to the feed sides of the membrane walls and withdrawal of filtrate liquid from the filtrate sides of said membrane walls; and

a pressure responsive valve in fluid communication with said pump, and configured to reverse the pressure differential applied to said membranes walls and to close in response to fluid pressure being applied to a control port.

2. The system according to claim 1, further including a filtrate vessel for receiving filtrate liquid withdrawn from the filtrate sides of said membranes.

3. The system according to claim 2, wherein the filtrate vessel is closed and the pump is operable to withdraw filtrate therefrom such that said withdrawal produces said pressure differential across said membranes walls.

4. The system according to claim 3, wherein the filtrate vessel is selectively closed by a gas stop valve, the gas stop valve being configured to allow gas to be vented from the filtrate vessel and configured to prevent entry of gas into the filtrate vessel.

5. The system according to claim 1, wherein an inlet of the pressure responsive valve is connected to an outlet of said pump, an outlet of the pressure responsive valve is coupled to said membrane filter device, and the control port is coupled to the outlet of said pump.

6. The system according to claim 5, further comprising a directional control valve having a first port, a second port, and an outlet port, wherein the directional control valve is configured to allow fluid flow from the first port to the outlet port while closing the second port responsive to a fluid pressure at the first port being higher than a fluid pressure at the second port and being configured to allow fluid flow from the second port to the first port while closing the outlet port responsive to the fluid pressure at the second port being higher than the fluid pressure at the first port.

7. The system according to claim 6, wherein the directional control valve is positioned between the pressure responsive valve and the membrane filter device, the outlet of the pressure responsive valve being connected to the second port, the membrane filter device being connected to the first port, and the outlet port being in fluid communication with the filtrate vessel.

8. The system according to claim 1, wherein the pump is operable to provide feed liquid under pressure to the feed sides of said membranes, the provision of the feed liquid under pressure to the feed sides of said membranes producing said pressure differential across the membrane walls.

9. The system according to claim 8, further comprising a further pump, the further pump configured to flow filtrate liquid from the filtrate sides of the membrane wall to the feed sides of the membrane wall, the flow of the filtrate liquid from the filtrate sides of the membrane wall to the feed sides of the membrane wall reversing the pressure differential applied to said membrane walls and effecting a backwash of the membranes.

10. The system according to claim 1, wherein the aerobic compost bed is formed in a feed vessel and said membrane filter device is in fluid communication with an inlet at or adjacent a base of said feed vessel.

11. The system according to claim 10, wherein said feed vessel includes a fluid level detection device configured to control the operation of said pump dependent on a level of liquid in said feed vessel.

12. The system according to claim 11, wherein said fluid level detection device is configured to disable the pump when the liquid level falls below a first predetermined limit, and to enable the pump when the liquid level rises to a second predetermined limit.

13. The system according to claim 12, wherein the first predetermined limit and second predetermined limit are the same.

14. The system according to claim 12 wherein the first predetermined limit is selected such that the inlet at or adjacent the base of the feed vessel remains immersed in liquid.

15. The system according to claim 10 wherein the inlet includes a foot valve.

16. A method of treating wastewater comprising:

forming and maintaining an aerobic compost bed in a feed vessel;

feeding wastewater onto the aerobic compost bed;

causing said wastewater to filter through the aerobic compost bed;

controlling operation of a pump with a fluid level switch located in the feed vessel;

removing filtered wastewater from the aerobic compost bed with the pump;

applying the removed filtered wastewater to a feed side of a membrane filter; and

withdrawing treated wastewater from a filtrate side of said membrane filter.

17. The method according to claim 16 further including the step of periodically backwashing the membrane filter by flowing treated wastewater back through the membrane filter from the filtrate side to the feed side.

18. The method according to claim 17 wherein the backwash step includes feeding backwash waste to the aerobic compost bed.

19. A method of operating a wastewater treatment system comprising:

providing a wastewater treatment system comprising a pressure responsive valve;

dropping a fluid pressure within a filtrate vessel during a filtration operation;

closing the pressure responsive valve during the filtration operation, the closing of the pressure responsive valve causing a fluid pressure at a first port of a directional control valve to exceed a fluid pressure at a second port of the directional control valve as the fluid pressure within the filtrate vessel drops;

flowing filtrate from a membrane filter device comprising one or more hollow, permeable membranes including walls having feed sides in fluid communication with an aerobic compost bed through the first port of the directional control valve and an outlet port of the directional control valve and into the filtrate vessel;

disabling a fluid pump when a feed liquid level in the aerobic compost bed falls below a first predetermined level;

releasing pressure from the pressure responsive valve in response to the disabling of the pump, the release of the pressure opening the pressure responsive valve;

enabling the fluid pump when the feed liquid level within the aerobic compost bed rises above a second predetermined level; and

applying a fluid pressure to the second port of the directional control valve which exceeds the pressure at the first port of the directional control valve in response to the enabling of the fluid pump, the application of the fluid pressure to the second port of the directional control valve causing the outlet port of the directional control valve to close and filtrate liquid to flow to filtrate sides of the membranes of the membrane filter device from the filtrate vessel through the second and first ports of the directional control valve.

20. The method of claim 19, further comprising backwashing the membranes of the membrane filter device by passing filtrate liquid through the membrane filter from the filtrate side to the feed side.

21. The method of claim 19, wherein flowing filtrate liquid to filtrate sides of the membranes of the membrane filter device from the filtrate vessel further comprises adding chlorine to the filtrate liquid flowed to the filtrate sides of the membranes of the membrane filter device from the filtrate vessel.