MEMBRANE CLEANING WITH PULSED GAS SLUGS

• US 20100300968A1
• Filed: 06/02/2010
• Published: 12/02/2010
• Est. Priority Date: 06/02/2009
• Status: Abandoned Application

• Current Assignee: Evoqua Water Technologies LLC (Xylem, Inc.)
• Original Assignee: Siemens Water Technologies Corp (Siemens AG)
• Inventors: Jordan, Edward, Liu, Wenjun
• Application Number:
  US12/792,307
• Publication Number:
  US 20100300968A1
• Time in Patent Office: Days
• US Class Current: 210/636
• CPC Class Codes: B01D 2311/16 Flow or flux control
• CPC Class Codes: B01D 2313/26 Specific gas distributors or gas intakes
• CPC Class Codes: B01D 2321/185 Aeration
• CPC Class Codes: B01D 2321/2066 Pulsated flow
• CPC Class Codes: B01D 61/18 Apparatus therefor
• CPC Class Codes: B01D 61/22 Controlling or regulating
• 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 1/008 Control or steering systems not provided for elsewhere in subclass C02F
• CPC Class Codes: C02F 2209/005 Processes using a programmable logic controller [PLC]
• CPC Class Codes: C02F 2209/03 Pressure
• CPC Class Codes: C02F 2209/40 Liquid flow rate
• CPC Class Codes: C02F 2303/16 Regeneration of sorbents, filters
• CPC Class Codes: C02F 3/1273 Submerged membrane bioreactors
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage

Abstract

Aspects and embodiments of the present application are direction to systems and methods for treating fluids and to systems and methods for cleaning membrane modules used in the treatment of fluids. Disclosed herein is a membrane filtration system and a method of operating same. The membrane filtration system comprises a plurality of membrane modules positioned in a feed tank, at least one of the membrane modules having a gas slug generator positioned below a lower header thereof, the gas slug generator configured and arranged to deliver a gas slug along surfaces of membranes within the at least one of the membrane modules and a global aeration system configured to operate independently from an aeration system providing a gas to the gas slug generator, the global aeration system configured and arranged to induce a global circulatory flow of fluid throughout the feed tank.

Claims

1. A membrane filtration system comprising:

a plurality of membrane modules positioned in a feed tank, at least one of the membrane modules having a gas slug generator positioned below a lower header thereof, the gas slug generator configured and arranged to deliver a gas slug along surfaces of membranes within the at least one of the membrane modules; and

a global aeration system configured to operate independently from an aeration system providing a gas to the gas slug generator, the global aeration system configured and arranged to induce a global circulatory flow of fluid throughout the feed tank.

2. The membrane filtration system of claim 1, further comprising:

a flow rate sensor configured to monitor a flow of permeate from the plurality of membrane modules; and

a controller, in communication with the flow rate sensor, configured to activate the global aeration system responsive to receiving a signal from the flow rate sensor indicative of a flow rate greater than a first amount and configured to deactivate the global aeration system responsive to receiving a signal from the flow rate sensor indicative of a flow rate less than a second amount.

3. The membrane filtration system of claim 2, wherein the plurality of membrane modules are arranged in racks, and wherein the global aeration system comprises gas diffusers configured to deliver gas between the racks of membrane modules.

4. The membrane filtration system of claim 3, wherein the gas diffusers are configured to deliver gas between adjacent membrane modules in a same rack.

5. The membrane filtration system of claim 4, wherein the gas diffusers are configured to deliver gas below the membrane modules.

6. The membrane filtration system of claim 2, wherein the controller is configured to activate the global aeration system when the flow rate is greater than about 25 liters per square meter of filtration membrane surface area per hour.

7. The membrane filtration system of claim 2, wherein the controller is configured to deactivate the global aeration system when the flow rate is less than about 25 liters per square meter of filtration membrane surface area per hour.

8. The membrane filtration system of claim 1, further comprising:

a transmembrane pressure sensor configured to monitor a pressure across the membranes of at least one of the membrane modules; and

a controller, in communication with the transmembrane pressure sensor, configured to activate the global aeration system responsive to receiving a signal from the transmembrane pressure sensor indicative of a transmembrane pressure greater than a first amount and configured to deactivate the global aeration system responsive to receiving a signal from the transmembrane pressure sensor indicative of a transmembrane pressure less than a second amount.

9. The membrane filtration system of claim 1, further comprising:

a feed flow rate sensor configured to monitor a flow rate of feed into the feed tank; and

a controller, in communication with the feed flow rate sensor, configured to activate the global aeration system responsive to receiving a signal from the feed flow rate sensor indicative of a flow rate of feed greater than a first amount and configured to deactivate the global aeration system responsive to receiving a signal from the feed flow rate sensor indicative of a flow rate of feed less than a second amount.

10. The membrane filtration system of claim 1, further comprising a timer configured to activate and deactivate the global aeration system at selected times.

11. A method of filtration comprising:

flowing a liquid medium into a filtration vessel including a plurality of membrane modules positioned therein, each of the membrane modules including an associated gas slug generator positioned below a lower end thereof;

withdrawing permeate from the plurality of membrane modules;

periodically delivering gas slugs from the gas slug generators into the membrane module associated with each gas slug generator, the gas slugs passing along membrane surfaces within each of the membrane modules to dislodge fouling materials therefrom; and

initiating and terminating a global circulatory flow through the filtration vessel responsive to signals derived from at least one of a permeate flow from the membrane modules, a feed flow into the filtration vessel in which the membrane modules are immersed, and a transmembrane pressure across the membranes of at least one of the membrane modules.

12. The method of claim 11, wherein a period of time between the delivery of gas slugs into each of the plurality of membrane modules is randomly determined.

13. The method of claim 12, further comprising providing each gas slug generator with an essentially constant supply of gas.

14. The method of claim 13, wherein initiating the global circulatory flow of feed comprises introducing gas into an aeration system operated independently of the gas slug generators.

15. The method of claim 14, wherein the gas slug generators and the aeration system are supplied with gas from a common source.

16. The method of claim 14, wherein initiating the global circulatory flow of feed further comprises initiating a pulsed flow of gas.

17. The method of claim 11, wherein initiating the global circulatory flow of feed comprises introducing gas between adjacent membrane modules of the plurality of membrane modules.

18. The method of claim 11, wherein the gas slugs are random in volume.

19. The method of claim 11, wherein the timing of the release of gas slugs into a first membrane module is independent of the timing of the release of gas slugs into a second membrane module.