DRAIN-FLUSH SEQUENCE AND SYSTEM FOR FILTER MODULE

• US 20080179244A1
• Filed: 01/26/2007
• Published: 07/31/2008
• Est. Priority Date: 01/26/2007
• Status: Abandoned Application

• Current Assignee: Parkson Corporation (BJA Croonen BV)
• Original Assignee: Parkson Corporation (BJA Croonen BV)
• Inventors: Ball, Andrew, Morgan, Charles R., Lebrun, Louis E.
• Application Number:
  US11/627,870
• Publication Number:
  US 20080179244A1
• Time in Patent Office: Days
• US Class Current: 210/636
• CPC Class Codes: B01D 2311/2688 Biological processes
• CPC Class Codes: B01D 2321/04 Backflushing
• CPC Class Codes: B01D 2321/10 Use of feed
• CPC Class Codes: B01D 2321/12 Use of permeate
• CPC Class Codes: B01D 2321/162 Use of acids
• CPC Class Codes: B01D 2321/164 Use of bases
• CPC Class Codes: B01D 2321/168 Use of other chemical agents
• CPC Class Codes: B01D 65/02 Membrane cleaning or sterilisation ; Membrane regeneration
• CPC Class Codes: C02F 2303/16 Regeneration of sorbents, filters
• CPC Class Codes: C02F 3/1268 Membrane bioreactor systems
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage

Abstract

The disclosed system and apparatus can be used to improve the operation of a membrane bioreactor wastewater treatment system. The system may include one or more membrane filtration modules having a proximal end and a distal end in which each module houses one or more membrane filters. The system and method can be configured to include the steps of interrupting the introduction or flow of feed liquid, allowing at least a portion of the feed liquid present in the one or more membrane filtration modules to drain therefrom, and to resume the introduction or feed of the feed liquid. Optionally, the system and method can include the step of allowing at least a portion of the recovered permeate to backflush the one or more membrane filters.

Claims

1. A method of operating a membrane bioreactor wastewater treatment system, which system comprises a bioreactor and one or more membrane filtration modules, each module having a proximal end and a distal end and housing a plurality of membrane filters, in which influent is introduced into the bioreactor and from which bioreactor a feed liquid is obtained which is introduced, in turn, to the proximal end of the one or more membrane filtration modules, a substantial portion of which feed liquid is recovered from the distal end thereof and returned to the bioreactor, but at least a portion of which feed liquid is allowed to pass from one side of said plurality of membrane filters and out an opposite side thereof to provide a permeate, said method comprising:

interrupting the introduction of said feed liquid to said proximal end of the one or more membrane filtration modules;

allowing at least a portion of said feed liquid present in the one or more membrane filtration modules to drain therefrom, along with at least a portion of any residue that might have accumulated on the said one side of said plurality of membrane filters; and

resuming the introduction of said feed liquid to said proximal end of the one or more membrane filtration modules.

2. The method of claim 1 in which the introduction of said feed liquid is interrupted by closing an input valve.

3. The method of claim 1 in which the at least a portion of said feed liquid is allowed to drain by the action of gravity.

4. The method of claim 2 in which the at least a portion of said feed liquid is allowed to drain by opening a drain valve.

5. The method of claim 1 which further comprises, prior to the resumption of the introduction of said feed liquid, flushing said plurality of membrane filters by causing at least a portion of said permeate to flow from said opposite side of said plurality of membrane filters and out the one side thereof or to flow from the one side of said plurality of membrane filters and out the opposite side thereof.

6. The method of claim 5 which further comprises introducing a first chemical solution to the one or more membrane filtration modules.

7. The method of claim 6 which further comprises introducing a second chemical solution to the one or more membrane filtration modules.

8. The method of claim 6 in which the first chemical solution comprises one or more hypochlorite, acid, caustic, surfactant, or any combination thereof.

9. The method of claim 7 in which the second chemical solution comprises one or more hypochlorite, acid, caustic, surfactant, or any combination thereof.

10. The method of claim 1 in which the introduction of said feed liquid is interrupted at least once for every 6 hours of continuous operation of the said membrane bioreactor wastewater treatment system.

11. A method of maintaining a membrane filtration module having a proximal end and a distal end, said module housing one or more tubular membrane filters through which a substantial portion of a feed liquid is allowed to flow into the proximal end and out the distal end of the membrane filtration module and in which at least a portion of the feed liquid is allowed to pass from one side of the one or more membrane filters and out an opposite side thereof to provide a permeate, the method comprising:

interrupting the flow of feed liquid;

allowing at least a portion of said feed liquid present in the membrane filtration module to drain therefrom, along with at least a portion of any residue that might have accumulated on one side of the one or more tubular membrane filters;

flushing the one or more tubular membrane filters by allowing an effective amount of permeate to flow from said opposite side of the one or more tubular membrane filters and out the one side thereof or to flow from said one side of the one or more tubular membrane filters and out said other opposite side thereof; and

resuming the flow of feed liquid.

12. The method of claim 11 in which an effective amount of permeate ranges from about 0.05×

to about 10×

the total volume of the membrane filtration module.

13. The method of claim 11 in which the flushing step is carried out during or after the at least a portion of said feed liquid is allowed to drain.

14. The method of claim 13 in which the at least a portion of said feed liquid is allowed to drain by opening a drain valve positioned below the one or more tubular membrane filters and opening a vent positioned above same.

15. A membrane wastewater filtration system comprising:

one or more membrane filtration modules having a proximal end and a distal end, each module housing one or more tubular membrane filters;

at least one inlet for introducing feed liquid;

at least one drain positioned below the one or more tubular membrane filters;

at least a first outlet for recycling a substantial portion of feed liquid introduced;

at least a second outlet for recovering permeate; and

at least one controller configured to (i) interrupt the introduction of feed liquid, (ii) allow at least a portion of feed liquid present in the one or more membrane filtration modules to drain therefrom, and (iii) allow at least a portion of recovered permeate to backflush the one or more tubular membrane filters.

16. The wastewater treatment system of claim 15 which further comprises a first pump for feeding the feed liquid to the at least one inlet and a circulation valve in fluid communication with the first pump, and

the controller is configured to close the circulation valve to interrupt the introduction of the feed flow.

17. The wastewater treatment system of claim 15 which further comprises a second pump in fluid communication with the second outlet and a draining valve in fluid communication with the at least one drain.

18. The wastewater treatment system of claim 17, in which the controller is configured to turn on the second pump while the draining valve is open.

19. The wastewater treatment system of claim 17, in which the controller is configured to close the draining valve before turning on the second pump.

20. The membrane wastewater filtration system of claim 17 which further comprises an air blower for introducing air in the vicinity of the proximal end of the one or more membrane filtration modules, and

the controller is configured to control the air blower to run while the draining valve is open, the second pump is in operation, or any combination thereof.

21. The wastewater treatment system of claim 17 which further comprises a chemical solution source and chemical flow valve in fluid communication with the second pump, and

the controller is configured to open the chemical flow valve and to operate the second pump.

22. The membrane wastewater filtration system of claim 15, which further comprises an air blower for introducing air in the vicinity of the proximal end of the one or more membrane filtration modules.

23. The membrane wastewater filtration system of claim 22 in which the air blower is configured to introduce air continuously.

24. The membrane wastewater filtration system of claim 22 in which the air blower is configured to introduce air intermittently.

25. The membrane wastewater filtration system of claim 22 in which the air blower is connected to the proximal end of the one or more membrane filtration modules through a delivery device, and in which the filtration system further comprises a cleaning device for flushing the delivery device with at least one of a liquid and an air stream.

26. The membrane wastewater filtration system of claim 22 in which the at least one controller is configured to automatically adjust an amount of air being blown by the air blower as a function of a membrane operating parameter.