Submerged cross-flow filtration

• US 7,591,950 B2
• Filed: 05/26/2006
• Issued: 09/22/2009
• Est. Priority Date: 11/02/2004
• Status: Active Grant

• Current Assignee: Evoqua Water Technologies LLC
• Original Assignee: Siemen Water Technologies Corporation (Siemens AG)
• Inventors: Zha, Fufang, Ganzi, Gary C., Beck, Thomas W.
• Primary Examiner(s): Fortuna; Ana M
• Application Number:
  US11/441,819
• Publication Number:
  US 20060273007A1
• Time in Patent Office: 1,215 Days
• Field of Search: 210/636, 210/650, 210/321.8, 210/321.69, 210/760, 210/321.9, 210/195.1, 210/257.2, 210/232
• US Class Current: 210/650
• CPC Class Codes: B01D 2313/23 Specific membrane protectors, e.g. sleeves or screens
• CPC Class Codes: B01D 2315/06 Submerged-type; Immersion type
• CPC Class Codes: B01D 2321/185 Aeration
• CPC Class Codes: B01D 2321/2016 Static mixers; Turbulence generators
• CPC Class Codes: B01D 61/18 Apparatus therefor
• CPC Class Codes: B01D 63/024 with a single potted end
• CPC Class Codes: B01D 63/043 with separate tube sheets
• 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

A membrane filtration module having a plurality of permeable, hollow membranes is disclosed. In use, a pressure differential is applied across the walls of the permeable, hollow membranes when immersed in a liquid suspension containing suspended solids. Some of the liquid suspension passes through the walls of the membranes to be drawn off as clarified liquid or permeate, and at least some of the solids are retained on or in the permeable, hollow membranes or otherwise as suspended solids within the liquid suspension. The module has a shell or similar structure that at least partially surrounds the membrane module and substantially effects retaining at least portion of fluid flowed into the membrane module.

Claims

1. A membrane filtration system comprising:

a vessel having an inlet fluidly connectable to a source of a liquid having solids suspended therein;

at least one membrane module disposed in the vessel, the membrane module comprising

a plurality of hollow fiber membranes extending between an upper potting head and a lower potting head, and a solid, non-porous sleeve surrounding the plurality of hollow fiber membranes, the upper potting head, and the lower potting head, and extending an entire length of the membrane module;

at least one scouring port fluidly connected to an aerator and to the source of the liquid;

a flow channel defined by the solid, non-porous sleeve, and the upper potting head, the lower potting head, and the plurality of hollow fiber membranes, said flow channel constructed and arranged to allow for the liquid to flow tangentially along the plurality of hollow fiber membranes, the upper potting head, and the lower potting head; and

a retentate exit port disposed adjacent to at least one of the lower potting head and the upper potting head, opposite the at least one scouring port.

2. The membrane filtration system of claim 1, wherein the membrane module further comprises a screen disposed adjacent an enclosed surface of the solid, non-porous sleeve.

3. The membrane filtration system of claim 1, further comprising a gas and liquid mixing chamber fluidly connected to at least one scouring port.

4. The membrane filtration system of claim 1, wherein at least one scouring port is disposed in an upper potting head of the membrane module.

5. The membrane filtration system of claim 1, wherein the solid, non-porous sleeve has a liquid exit port medially disposed between the upper potting head and the lower potting head.

6. The membrane module of claim 1, wherein at least one scouring port is disposed in the lower potting head.

7. The membrane module of claim 1, wherein the scouring fluid further comprises suspended solids.

8. The membrane module of claim 1, further comprising baffle at least one disposed within the solid, non-porous sleeve.

9. A membrane module comprising:

a plurality of hollow fiber membranes extending between an upper potting head and a lower potting head;

means for introducing a scouring fluid to the plurality of hollow fiber membranes fluidly connected to an aerator and to a source of a liquid;

a solid, non-porous sleeve surrounding the plurality of hollow fiber membranes, the upper potting head, and the lower potting head, and extending an entire length of the membrane module;

a flow channel defined by the solid, non-porous sleeve, and the upper potting head, the lower potting head, and the plurality of hollow fiber membranes, said flow channel constructed and arranged to allow for a fluid to flow tangentially along the plurality of hollow fiber membranes, the upper potting head, and the lower potting head; and

a retentate exit port disposed adjacent to at least one of the lower potting head and the upper potting head, opposite the means for introducing a scouring fluid.

10. The membrane module of claim 9, wherein the plurality of fiber membranes are arranged in at least two bundles each defining a sub-module.

11. The membrane module of claim 10, further comprising a baffle plate disposed between at least two sub-modules.

12. The membrane module of claim 11, further comprising means for adjusting a gas to a liquid ratio of the scouring fluid.

13. A method of purifying water having solids suspended therein, comprising:

introducing the water to be purified through a first end of a flow channel of a membrane module comprising a solid sleeve surrounding a plurality of hollow fiber membranes, a lower potting head, and an upper potting head, and extending an entire length of the membrane module, the solid sleeve defining the flow channel for the water to flow tangentially along the lower potting head, the upper potting head, and the plurality of hollow fiber membranes, and the membrane module having a retentate exit port disposed adjacent to at least one of the lower potting head and the upper potting head;

introducing a scouring fluid comprising a mixture of a gas and a liquid into the flow channel by an aerator fluidly connected to a source of a liquid;

withdrawing permeate through the hollow fiber membranes and an exit port in at least one of the lower potting head and the upper potting head; and

withdrawing retentate through the flow channel at an end opposite the first end of the membrane module.

14. The method of claim 13, wherein the scouring fluid further comprises suspended solids.

15. The method of claim 13, wherein the scouring fluid is introduced into the volume through at least one scouring port disposed in at least one of the lower potting head and the upper potting head.

16. The method of claim 13, further comprising withdrawing retentate through the retentate exit port and introducing the withdrawn retentate to a second membrane module.

17. The method of claim 13, further comprising introducing a second scouring fluid into the volume.

18. The membrane module of claim 13, wherein at least one scouring port is disposed in the upper potting head.

19. The method of claim 13, wherein withdrawing permeate through the hollow fiber membranes comprises suctioning off permeate from an inner permeate side of the membrane module.