Membrane filter cleansing process

• US 20060065596A1
• Filed: 10/12/2004
• Published: 03/30/2006
• Est. Priority Date: 09/24/2004
• Status: Abandoned Application

• Current Assignee: Zenon Technology Partnership
• Original Assignee: Zenon Technology Partnership
• Inventors: Ross, David Brian, Kent, Fraser Charles
• Application Number:
  US10/961,077
• Publication Number:
  US 20060065596A1
• Time in Patent Office: Days
• US Class Current: 210/636
• CPC Class Codes: B01D 2315/06 Submerged-type; Immersion type
• CPC Class Codes: B01D 2321/04 Backflushing
• CPC Class Codes: B01D 2321/185 Aeration
• CPC Class Codes: B01D 63/02 Hollow fibre modules
• CPC Class Codes: B01D 65/02 Membrane cleaning or sterilisation ; Membrane regeneration
• CPC Class Codes: B01D 65/08 Prevention of membrane fouling or of concentration polarisation
• CPC Class Codes: C02F 1/444 by ultrafiltration or microfiltration

Abstract

Immersed hollow-fiber membrane filtration systems sometimes encounter process problems as a result of solids accumulation in and around the hollow fibers. The solids can accumulate to the point where they begin to dewater and form a mud like substance known as sludge. In some embodiments of the invention there is provided a process for substantially preventing the accumulation of sludge build-up on membrane fibers and/or cleansing membrane fibers that have been fouled by a substantial sludge build-up. Many of these embodiments involve aerating a membrane tank in which the membrane fibers are immersed after the water level has been reduced to near the level of solids accumulation. In some embodiments of the invention, the energy released by bursting bubbles at the liquid-air interface is employed to prevent fouling of membrane fibers and/or cleanse fouled membrane fibers.

Claims

1. A process for removing solids from a module of membrane fibers immersed in a liquid comprising:

(a) reducing the level of the liquid to a level corresponding to an area of the membrane fibers having an accumulation of solids; and

,

(b) providing aeration for a period of time while the liquid is at the level corresponding to the area of the membrane fibers having the accumulation of solids in order to dislodge at least a portion of the solids from the membrane fibers.

2. A process according to claim 1 further comprising, after step (b), draining the remaining liquid.

3. A process according to claim 1 further comprising re-immersing the membrane fibers after step (b) of claim 1.

4. A process according to claim 1, wherein the liquid level at step (b) of claim 1 is near the bottom header of a module of vertically oriented fibers.

5. A process according to claim 1 wherein the liquid level at step (b) of claim 1 is within 30 cm of the top of the lower header of a module of vertically oriented hollow fibers

6. A process according to claim 1, wherein step (b) is provided for between about 30 seconds and 20 minutes.

7. A process according to claim 1, wherein the steps occur in less than 30 minutes.

8. A process according to claim 1 wherein the steps occur in less than 15 minutes.

9. A process according to claim 1, wherein the steps of claim 1 are incorporated into the regular operation of a batch filtering system having a cycle of permeation and deconcentration by using the steps of claim 1 to provide a deconcentration.

10. A process according to claim 1 wherein the membranes are aerated during step (a).

11. A process according to claim 1 further comprising, after step (b) of claim 1,

(c) reducing the level of the liquid to a second level corresponding to an area of the membrane fibers having an accumulation of solids;

and,

(d) providing aeration for a period of time while the liquid is at the second level corresponding to the areas of the membrane fibers having the accumulation of solids in order to dislodge at least a portion of the solids from the membrane fibers.