LOW PRESSURE BACKWASH

• US 20090255873A1
• Filed: 08/30/2007
• Published: 10/15/2009
• Est. Priority Date: 08/31/2006
• Status: Abandoned Application

• Current Assignee: Evoqua Water Technologies LLC (Xylem, Inc.)
• Original Assignee: Evoqua Water Technologies LLC (Xylem, Inc.)
• Inventors: Ly, Lyvonne, Zha, Fufang, Cao, Zhiyi, Biltoft, Bruce Gregory, Lazaredes, Huw Alexander
• Application Number:
  US12/439,209
• Publication Number:
  US 20090255873A1
• Time in Patent Office: Days
• US Class Current: 210/636
• CPC Class Codes: B01D 2311/14 Pressure control
• CPC Class Codes: B01D 2313/24 Specific pressurizing or depressurizing means
• CPC Class Codes: B01D 2321/04 Backflushing
• CPC Class Codes: B01D 2321/12 Use of permeate
• CPC Class Codes: B01D 2321/2066 Pulsated flow
• 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 method of backwashing a membrane filtration system comprising at least one permeable hollow membrane, the method comprising the step of applying a low-pressure gas to the permeate remaining present in the system when the filtration process is stopped or suspended to provide liquid for backwashing the pores of the membrane during a backwashing process.

Claims

1. A method of backwashing a membrane filtration system comprising at least one permeable hollow membrane, the method comprising the step of applying a low-pressure gas to the permeate remaining present in the filtration system when the filtration process is stopped or suspended to provide liquid for backwashing pores of the membrane during a backwashing process, wherein the low-pressure gas is at a pressure in the range of about 30 kPa to about 150 kPa.

2. A method according claim 1 wherein the low-pressure gas is at a pressure below the bubble point of the membrane.

4. A method according to claim 1 wherein the low-pressure gas is provided by one or more gas pressure pulses.

3. (canceled)

5. A method of filtering solids from a liquid suspension comprising:

(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) permeable 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) periodically backwashing the membrane pores using the permeate remaining within the lumens by applying low pressure gas at a pressure below the bubble point of the membrane to said liquid permeate to displace at least some of the liquid permeate within the lumens through the membrane pores resulting in removal of the solids retained on or in the hollow membranes, wherein the low-pressure gas is at a pressure in the range of about 30 kPa to about 150 kPa.

7. A method according to claim 5 wherein, during the backwashing step, the solids are removed into the bulk liquid surrounding the membranes.

8. A method according to claim 5 wherein permeate remaining in ancillaries is used as a source of backwash liquid.

9. A method according to claim 5 further comprising providing a further chamber or reservoir in a permeate flow circuit to increase the amount of permeate available for backwashing.

10. A method according to claim 5 wherein the permeate is withdrawn from both ends of the membrane lumens and wherein the low pressure gas is applied to one or both ends of the membrane lumens during the backwashing step.

11. A method according to claim 5 wherein the low-pressure gas is provided by one or more gas pressure pulses.

12. A method according to claim 11 wherein the pressure pulse or pulses are provided by isolating the liquid suspension side of the membranes during the backwashing step while applying low pressure gas to both the liquid suspension side and the permeate side of the membranes to pressurize the liquid suspension and permeate sides of the membranes, then opening the liquid suspension side of the membranes to atmosphere resulting in a depressurisation of the liquid suspension side and the application of a pulse of pressure to the permeate side of the membranes.

6. A method of filtering solids from a liquid suspension in a filtration system comprising:

(i) providing a pressure differential across the walls of permeable, hollow membranes having a liquid suspension applied to the inner surface of the permeable 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 outer surface of said membranes, and

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

(ii) stopping or suspending the filtration process;

(iii) periodically backwashing the membrane pores using the permeate remaining in the system after the suspension of the filtration process by applying a low pressure gas at a pressure below the bubble point of the membrane to said liquid permeate to displace at least some of the liquid permeate through the membrane pores resulting in removal of the solids retained on or in the hollow membranes wherein the low-pressure gas is at a pressure in the range of about 30 kPa to about 150 kPa.

13. A filtration system for removing fine solids from a liquid suspension comprising:

(i) a vessel for containing said liquid suspension;

(ii) a plurality of permeable, hollow membranes within the vessel;

(iii) means for providing a pressure differential across walls of said membranes such that some of the liquid suspension passes through the walls of the membranes to be drawn off as permeate;

(iv) means for withdrawing permeate from the membranes; and

(v) means for applying low pressure gas at a pressure below the bubble point to the liquid permeate within the system and the membrane lumens to cause a discharge of at least some of the liquid permeate in the lumens through the membrane walls to dislodge any solids retained therein and displace the removed solids into the liquid suspension surrounding the membranes, wherein the low-pressure gas is at a pressure in the range of about 30 kPa to about 150 kPa.

14. A filtration system according to claim 13 wherein the low-pressure gas is provided by one or more gas pressure pulses.

15. A filtration system according to claim 13 wherein the low-pressure gas is provided from a source of gas used to aerate the membranes.

16. A filtration system according to claim 13 wherein the gas pressure is regulated by a control valve or pressure-limiting device.

17. A filtration system according to claim 13 wherein the low-pressure gas is employed to push the remaining permeate through pores of the membrane wall.

20. A filtration system according to claim 13 wherein the low pressure is provided from a blower used for gas scouring of the membrane.

21. A filtration system according to claim 13 further comprising a number of the membrane modules, each membrane module comprising one or more of the membranes, wherein the membrane modules are arranged in a bank and connected to a manifold for distributing liquid suspension to the membrane modules and removing permeate therefrom, and wherein the low pressure gas is introduced into the manifold of the bank of membrane modules so that the permeate in the manifold forms part of the permeate within the system.

18-19. -19. (canceled)

22. A method of backwashing a membrane filtration system comprising at least one permeable hollow membrane, the method comprising the step of applying a low-pressure gas to the permeate remaining present in the filtration system when the filtration process is stopped or suspended to provide liquid for backwashing pores of the membrane during a backwashing process, wherein the low-pressure gas is provided by one or more gas pressure pulses.

23. A method of filtering solids from a liquid suspension comprising:

(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 permeable 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) periodically backwashing the membrane pores using the permeate remaining within the lumens by applying low pressure gas at a pressure below the bubble point of the membrane to said liquid permeate to displace at least some of the liquid permeate within the lumens through the membrane pores resulting in removal of the solids retained on or in the hollow membranes, wherein the low-pressure gas is provided by one or more gas pressure pulses.

24. A method of filtering solids from a liquid suspension in a filtration system comprising:

(i) providing a pressure differential across the walls of permeable, hollow membranes having a liquid suspension applied to the inner surface of the permeable 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 outer surface of said membranes, and

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

(ii) stopping or suspending the filtration process;

(iii) periodically backwashing the membrane pores using the permeate remaining in the system after the suspension of the filtration process by applying a low pressure gas at a pressure below the bubble point of the membrane to said liquid permeate to displace at least some of the liquid permeate through the membrane pores resulting in removal of the solids retained on or in the hollow membranes, wherein the low-pressure gas is provided by one or more gas pressure pulses.

25. A filtration system for removing fine solids from a liquid suspension comprising:

(i) a vessel for containing said liquid suspension;

(ii) a plurality of permeable, hollow membranes within the vessel;

(iii) means for providing a pressure differential across walls of said membranes such that some of the liquid suspension passes through the walls of the membranes to be drawn off as permeate;

(iv) means for withdrawing permeate from the membranes; and

(v) means for applying low pressure gas at a pressure below the bubble point to the liquid permeate within the system and the membrane lumens to cause a discharge of at least some of the liquid permeate in the lumens through the membrane walls to dislodge any solids retained therein and displace the removed solids into the liquid suspension surrounding the membranes, wherein the low-pressure gas is provided by one or more gas pressure pulses.