Continuous pressure decay test

• US 20070056905A1
• Filed: 02/18/2005
• Published: 03/15/2007
• Est. Priority Date: 02/18/2004
• Status: Abandoned Application

• Current Assignee: Siemen Water Technologies Corporation (Siemens AG)
• Original Assignee: US Filter Wastewater Group Incorporated (Siemens AG)
• Inventors: Johnson, Warren, Beck, Thomas
• Application Number:
  US10/597,903
• Publication Number:
  US 20070056905A1
• 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 2321/18 Use of gases
• CPC Class Codes: B01D 63/024 with a single potted end
• CPC Class Codes: B01D 65/02 Membrane cleaning or sterilisation ; Membrane regeneration
• CPC Class Codes: B01D 65/102 Detection of leaks in membranes

Abstract

A continuous integrity test is performed on membranes in a membrane filtration system during the backwashing phase. The membrane pores are backwashed by applying a gas at a pressure below the bubble point to liquid permeate within the membrane lumens to displace the liquid permeate within the lumens through the membrane pores. An integrity test is performed on the membranes by allowing the gas pressure on the lumen side of the membrane walls to increase to a predetermined level above the pressure on the other side of the membrane walls, then isolating the lumen side of the membranes and measuring the reduction in gas pressure on the lumen side of the membrane walls resulting from gas passing through the membrane walls over a predetermined period. The measured reduction in pressure is then compared against a predetermined value to determine the integrity of said membranes.

Claims

1. A method of testing the integrity of permeable hollow membranes used for filtering solids from a liquid suspension including:

(i) providing a pressure differential across the walls of permeable, hollow membranes immersed in the liquid suspension, said liquid suspension being applied to the outer surface of the porous hollow membranes to induce and sustain filtration through the membrane walls wherein;

(a) some of the liquid suspension passes through the walls of the membranes to be drawn off as permeate from the hollow membrane lumens, and

(b) at least some of the solids are retained on or in the hollow membranes or otherwise as suspended solids within the liquid surrounding the membranes,

(ii) backwashing the membrane pores by applying a gas at a pressure below the bubble point to liquid permeate within the membrane lumens to displace the liquid permeate within the lumens through the membrane pores,

(iii) performing an integrity test on the membranes by

a. allowing the gas pressure on the lumen side of the membrane walls to increase to a predetermined level above the pressure on the other side of the membrane walls,

b. isolating the lumen side of the membranes,

c. measuring the reduction in gas pressure on the lumen side of the membrane walls resulting from gas passing through the membrane walls over a predetermined period,

d. comparing the measured reduction in pressure against a predetermined value to determine the integrity of said membranes,

(iv) refilling membrane lumens with liquid, and

(v) recommencing said filtration through the membrane walls.

2. A method of testing the integrity of permeable hollow membranes used for filtering solids from a liquid suspension according to claim 1 wherein the integrity is tested during each backwash of the membranes.

3. A method of testing the integrity of permeable hollow membranes used for filtering solids from a liquid suspension according to claim 1 wherein the integrity is tested after a predetermined number of backwashes of the membranes.

4. A method of testing the integrity of permeable hollow membranes used for filtering solids from a liquid suspension according to claim 1 wherein said predetermined value corresponds to a logarithmic reduction value of 4.