MEMBRANE FILTRATION SYSTEM

• US 20110315632A1
• Filed: 05/24/2011
• Published: 12/29/2011
• Est. Priority Date: 05/24/2010
• Status: Abandoned Application

• Current Assignee: Peter L. Freije, William F. Freije III
• Original Assignee: Peter L. Freije, William F. Freije III
• Inventors: Freije, William F. III, Freije, Peter L.
• Application Number:
  US13/141,562
• Publication Number:
  US 20110315632A1
• Time in Patent Office: Days
• US Class Current: 210/636
• CPC Class Codes: B01D 2321/16 Use of chemical agents
• CPC Class Codes: B01D 61/12 Controlling or regulating
• CPC Class Codes: B01D 61/22 Controlling or regulating
• CPC Class Codes: B01D 65/02 Membrane cleaning or sterilisation ; Membrane regeneration

Abstract

A membrane system is disclosed. The membrane system may include a treatment process wherein both at least a portion of a permeate output of the membrane system and a concentrate output of the membrane system are recirculated back to an input of the membrane system. The membrane system may include a treatment process wherein a higher level permeate is used to treat the membrane system. The membrane system may include a storage reservoir to store at least a portion of the concentrate output of a purge cycle of the membrane system.

Claims

1. A method of operating a membrane system which receives a fluid at an input of the membrane system and provides a permeate output and a concentrate output;

the method comprising the steps of;

receiving at least a portion of a permeate output from the membrane system;

receiving at least a portion of a concentrate output from the membrane system;

recirculating both the received portion of the permeate output of the membrane system and the received portion of the concentrate output of the membrane system back to the input of the membrane system; and

passing together the received portion of the permeate output of the membrane system and the received portion of the concentrate output of the membrane system through the membrane system.

2. The method of claim 1, wherein the step of recirculating both the received portion of the permeate output of the membrane system and the received portion of the concentrate output of the membrane system back to the input of the membrane system includes the steps of:

passing the received portion of the concentrate output of the membrane system through a fluid conduit which is in fluid communication with the input of the membrane system; and

passing the received portion of the permeate output of the membrane system through the fluid conduit along with the received portion of the concentrate output of the membrane system.

3. The method of claim 1, wherein the step of recirculating both the received portion of the permeate output of the membrane system and the received portion of the concentrate output of the membrane system back to the input of the membrane system includes the steps of:

directing the received portion of the permeate output of the membrane system to a storage reservoir;

directing the received portion of the concentrate output of the membrane system to the storage reservoir; and

directing at least a portion of the fluid from the storage reservoir to the input of the membrane.

4. The method of claim 1, wherein the steps of claim 1 comprise a closed loop recirculation process.

5. A method of operating a membrane system which receives a fluid at an input and provides a permeate output and a concentrate output;

the method comprising the steps of;

providing a cleaning fluid to the input of the membrane system;

passing the cleaning fluid through the membrane system;

mixing at least a portion of the concentrate output produced by the membrane system from the cleaning fluid with at least a portion of the permeate output produced by the membrane system from the cleaning fluid; and

passing at least a portion of the mixture through the membrane system.

6. The method of claim 5, wherein the step of mixing at least the portion of the concentrate output produced by the membrane system from the cleaning fluid with at least the portion of the permeate output produced by the membrane system from the cleaning fluid includes the steps of:

directing at least the portion of the concentrate output produced by the membrane system from the cleaning fluid to a storage reservoir; and

directing at least the portion of the permeate output produced by the membrane system from the cleaning fluid to the storage reservoir.

7. The method of claim 5, wherein the steps of claim 5 comprise a closed loop recirculation process.

8. The method of claim 5, wherein the step of mixing at least the portion of the concentrate output produced by the membrane system from the cleaning fluid with at least the portion of the permeate output produced by the membrane system from the cleaning fluid includes the steps of:

directing at least the portion of the concentrate output produced by the membrane system from the cleaning fluid to a fluid conduit in fluid communication with the input of the membrane system; and

directing at least the portion of the permeate output produced by the membrane system from the cleaning fluid to the fluid conduit in fluid communication with the input of the membrane system.

9-19. -19. (canceled)

20. A method of operating a membrane system which receives a fluid at an input of the membrane system and provides a permeate output and a concentrate output;

the method comprising the steps of;

(a) performing a first run cycle with the membrane system, wherein a first input fluid is separated into a first permeate fluid and a first concentrate fluid and wherein materials from the first input fluid are left within the membrane system;

(b) performing a purge cycle of the membrane system by passing a first cleaning fluid through the membrane system;

(c) performing a secondary purge cycle of the membrane system by passing a second cleaning fluid through the membrane system, the second cleaning fluid includes at least about 10% of a higher level permeate;

(d) recirculating both a portion of a permeate output fluid of the secondary purge cycle and a portion of a concentrate output fluid of the secondary purge cycle back to the input of the membrane; and

(e) performing a second run cycle with the membrane system, wherein a second input fluid is separated into a second permeate fluid and a second concentrate fluid, the second input fluid including at least a portion of a concentrate fluid produced during at least one of steps (b)-(d).

21. The method of claim 20, wherein the first cleaning fluid includes at least a portion of the first permeate fluid produced during the run cycle.

22. The method of claim 20, wherein the first cleaning fluid includes the first input fluid.

23. The method of claim 20, wherein the second cleaning fluid includes at least about 50% of a higher level permeate.

24. The method of claim 20, wherein the second cleaning fluid includes at least about 80% of a higher level permeate.

25. The method of claim 20, wherein the second cleaning fluid includes at least about 90% of a higher level permeate.

26. The method of claim 20, wherein the second cleaning fluid includes between about 10% to about 100% of a higher level permeate.

37. The method of claim 20, further comprising the step of retaining at least a portion of the first cleaning fluid exiting the membrane system during the purge cycle for injection into the membrane system during a subsequent run cycle.

38. The method of claim 20, further comprising the steps of:

providing a purge reservoir;

providing a non-potable permeate storage reservoir;

providing a potable permeate storage reservoir; and

wherein the first input fluid is provided in the non-potable permeate storage reservoir and the non-potable permeate storage reservoir is placed in fluid communication with the input of the membrane system during step (a).

39. The method of claim 20, further comprising the steps of:

providing a purge reservoir;

providing a non-potable permeate storage reservoir;

providing a potable permeate storage reservoir; and

wherein the first input fluid is provided in the purge reservoir and the purge reservoir is placed in fluid communication with the input of the membrane system during step (a).

27-36. -36. (canceled)