Membrane batch filtration process

• US 20050194315A1
• Filed: 02/22/2005
• Published: 09/08/2005
• Est. Priority Date: 02/27/2004
• Status: Abandoned Application

• Current Assignee: Zenon Environmental Incorporated (Veolia Environnement SA)
• Original Assignee: Zenon Environmental Incorporated (Veolia Environnement SA)
• Inventors: Singh, Manwinder, Cote, Pierre Lucien, Adams, Nicholas William Harcsar, Dufresne, Kevin Simon Joseph
• Application Number:
  US11/061,629
• Publication Number:
  US 20050194315A1
• Time in Patent Office: Days
• US Class Current: 210/636
• CPC Class Codes: B01D 2315/20 Operation control schemes defined by a periodically repeated sequence comprising filtration cycles combined with cleaning or gas supply, e.g. aeration
• CPC Class Codes: B01D 61/22 Controlling or regulating
• CPC Class Codes: B01D 65/02 Membrane cleaning or sterilisation ; Membrane regeneration
• 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 2303/16 Regeneration of sorbents, filters

Abstract

A membrane batch filtration process has a step of reducing the water level in the tank by permeation prior to emptying the tank to reduce the volume of water drained after each batch. Permeation may continue even after a portion of the membranes is exposed to air to further lower the water level. The membranes may be backwashed after the water level has been lowered. The water level may be lowered again after the backwash. The tank drain may begin with a portion of the membranes exposed to air.

Claims

1. A batch membrane filtration process comprising the steps, performed in repeated cycles, of:

a) filling a tank to immerse membranes in the tank;

b) after step (a), withdrawing permeate through the membranes while adding feed to keep the membranes immersed;

c) after step (b), withdrawing permeate while the flow of feed is reduced or stopped to lower the water level in the tank;

d) backwashing the membranes; and

,

e) after steps (a), (b) and (c), draining the tank.

2. The process of claim 1 wherein step (d) occurs after step (c) and before step (e).

3. The process of claim 1 wherein, in step (c), the water level in the tank is lowered to a point where a portion of the membranes are exposed to air.

4. The process of claim 3 wherein the volume of water provided during step (d) re-immerses the portion of the membranes exposed to air.

5. The process of claim 4 wherein the membranes are scoured with air as or after the portion of the membranes is re-immersed.

6. The process of claim 2 wherein step (c) is repeated after step (d) and before step (e).

7. The process of claim 1 wherein step (d) occurs after step (e).

8. The process of claim 7 wherein, after step (d), step (e) is repeated before returning to step (a).

9. The process of claim 8 wherein step (c) is repeated after step (d) and before step (e) is repeated.

10. The process of claim 1 wherein the membranes are scoured with air before, during or between any of steps (c), (d) or (e).

11. The process of claim 1 wherein step (d) is performed before step (c).

12. A batch membrane filtration process wherein the tank is drained starting at a time when the water level has been lowered by permeation to expose a portion of the membranes to air.

13. A reactor having a membrane tank with a membrane module and an overflow area, the overflow area being fluidly connected to the tank through a valved passageway from the bottom of the overflow area to the tank such that the overflow area can drain into the tank, the passageway located below the top of the membrane module.

14. The reactor of claim 13 having a passageway between the tank and the overflow area, the overflow located above the passageway and above the top of the membrane module.