IP Library Granted Patent US 9,573,824
Granted Patent B2
US 9,573,824 · App. 14/090,491 · Granted Feb 21, 2017

Membrane cleaning with pulsed airlift pump

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Quick Facts
Patent No.
US 9,573,824
App. No.
14/090,491
Granted
Feb 21, 2017
Kind
B2
Abstract

A method of cleaning a membrane surface immersed in a liquid medium with a fluid flow, including the steps of providing a randomly generated intermittent or pulsed fluid flow along the membrane surface to dislodge fouling materials therefrom. A membrane module is also disclosed comprising a plurality of porous membranes ( 6 ) or a set of membrane modules ( 5 ) and a device ( 11 ) for providing a generally randomly generated, pulsed fluid flow such that, in use, said fluid flow moves past the surfaces of said membranes ( 6 ) to dislodge fouling materials therefrom.

Claims (28)

1. A method of cleaning a membrane module in an array of membrane modules immersed in a liquid feed tank, the module comprising a plurality of membrane bundles, the method comprising:

applying a pressurized gas to a gas collection chamber of a gas-lift pump device positioned below the membrane bundles of the module, a single gas-lift pump device positioned below each single module in the array of membrane modules and each single module in the array of membrane modules associated with a single gas-lift pump, wherein, the gas applied to the gas collection chamber displaces feed liquid within the chamber until the gas reaches an opening in a central riser tube that extends through the gas collection chamber and has a first end in fluid communication with the membrane bundles and a second end fluidly connected to the liquid feed tank,

whereupon a surge of gas passes through the opening and creates a bubble slug that flows into the membrane module, the surge of gas providing

an ejection phase, which ejects gas and feed liquid through the first end of the riser tube to the membrane module to clean the plurality of membrane bundles, and

a suction phase, which creates a reduction in pressure and pulls feed liquid through the second end of the riser tube.

2. The method of claim 1 , wherein applying the pressurized gas comprises applying a continuous source of gas.

3. The method of claim 1 , wherein a tubular trough having an open upper end and a closed lower end extends around and upward from the central riser tube, the closed lower end positioned below the opening of the central riser tube, wherein the trough prevents immediate resealing of the opening.

4. The method of claim 1 , further comprising applying a pressurized gas from an additional source of gas to an additional opening in the central riser tube.

5. The method of claim 4 , wherein the additional source of gas is constantly applied to generate a constant flow of gas and feed liquid to the membrane module.

6. The method of claim 1 , further comprising filtering the feed liquid through the plurality of membrane bundles to produce a filtrate.

7. The method of claim 6 , further comprising applying the pressurized gas while filtering the feed liquid.

8. The method of claim 1 , further comprising removing fouling materials from surfaces of membranes of the membrane bundles using the surge of gas.

9. The method of claim 1 , wherein the bubble slug passes through a distribution chamber positioned between the gas collection chamber and the plurality of membrane bundles.

10. The method of claim 1 , wherein the suction phase further draws gas through the opening in the central riser tube.

11. The method of claim 1 , wherein the plurality of membrane bundles are cleaned and a decrease in membrane permeability is lower than a decrease in membrane permeability when cleaning a plurality of membrane bundles using cyclic aeration.

12. The method of claim 11 , wherein the cyclic aeration includes repeated cycles where the pressurized gas is applied for a duration of 10 seconds, followed by a duration of 10 seconds where the pressurized gas is turned off.

13. The method of claim 11 , wherein the cyclic aeration includes repeated cycles where the pressurized gas is applied for a duration of 3 seconds, followed by a duration of 3 seconds where the pressurized gas is turned off.

14. The method of claim 1 , wherein the ejection phase and the suction phase create a cycle pattern and the method further comprises repeating the cycle pattern.

15. The method of claim 14 , wherein each cycle pattern is different from another cycle pattern in at least one of duration, frequency, and intensity.

16. The method of claim 14 wherein each cycle pattern generates a different flow profile than another cycle pattern.

17. The method of claim 1 , wherein each membrane module in the array of membrane modules comprises a plurality of membrane bundles and a central riser tube positioned below the plurality of membrane bundles.

18. The method of claim 1 , wherein the membrane module comprises a single gas collection chamber positioned below the plurality of the membrane bundles.

19. The method of claim 1 , wherein pulses of gas bubbles produced by each gas-lift pump device occur randomly for each module, resulting in an overall random distribution of pulsed gas bubble generation within the feed tank.

20. A method of cleaning a membrane module immersed in a liquid feed tank, the module comprising a plurality of membrane bundles mounted in and extending from a lower potting head, the lower potting head having openings to allow flow of fluids therethrough from a distribution chamber positioned below the lower potting head, the method comprising:

applying a pressurized gas to a gas collection chamber positioned below the distribution chamber, wherein the gas applied to the gas collection chamber displaces feed liquid within the chamber until the gas reaches an opening in a central riser tube that extends through the gas collection chamber and has a first end fluidly connected to a base of the distribution chamber and a second end fluidly connected to the liquid feed tank,

whereupon a surge of gas passes through the opening and creates a bubble slug that flows through the distribution chamber and into the membrane module through the openings in the lower potting head, the surge of gas providing

an ejection phase, which ejects gas and feed liquid through the first end of the riser tube to the membrane module to clean the plurality of membrane bundles, and

a suction phase, which creates a reduction in pressure and pulls feed liquid through the second end of the riser tube.

Assignments (5)
RELEASE OF SECURITY INTEREST (REEL/FRAME 032126/0487) Recorded Apr 6, 2021
From: CREDIT SUISSE AG, CAYMAN ISLANDS BRANCH, AS COLLATERAL AGENT
To: SIEMENS WATER TECHNOLOGIES LLC
Reel/Frame 055845/0245 →
RELEASE OF SECURITY INTEREST (REEL/FRAME 032126/0430) Recorded Apr 6, 2021
From: CREDIT SUISSE AG, CAYMAN ISLANDS BRANCH, AS COLLATERAL AGENT
To: SIEMENS WATER TECHNOLOGIES LLC
Reel/Frame 055845/0311 →
CHANGE OF NAME Recorded Feb 7, 2014
From: SIEMENS WATER TECHNOLOGIES LLC
To: EVOQUA WATER TECHNOLOGIES LLC
Reel/Frame 032173/0401 →
INTELLECTUAL PROPERTY SECURITY AGREEMENT (SECOND LIEN) Recorded Jan 24, 2014
From: WTG HOLDINGS III CORP.; WTG HOLDINGS II CORP.; SIEMENS TREATED WATER OUTSOURCING CORP.; SIEMENS WATER TECHNOLOGIES LLC
To: CREDIT SUISSE AG, CAYMAN ISLANDS BRANCH, AS COLLATERAL AGENT
Reel/Frame 032126/0430 →
INTELLECTUAL PROPERTY SECURITY AGREEMENT (FIRST LIEN) Recorded Jan 24, 2014
From: WTG HOLDINGS III CORP.; WTG HOLDINGS II CORP.; SIEMENS TREATED WATER OUTSOURCING CORP.; SIEMENS WATER TECHNOLOGIES LLC
To: CREDIT SUISSE AG, CAYMAN ISLANDS BRANCH, AS COLLATERAL AGENT
Reel/Frame 032126/0487 →