Apparatus for withdrawing permeate using an immersed vertical skein of hollow fibre membranes

• US 20070007207A1
• Filed: 09/19/2006
• Published: 01/11/2007
• Est. Priority Date: 08/11/1995
• Status: Active Grant

• Current Assignee: Zenon Technology Partnership
• Original Assignee: Zenon Technology Partnership
• Inventors: Pedersen, Steven, Mahendran, Malivaganam
• Granted Patent: US 7,708,888 B2
• 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 2321/12 Use of permeate
• 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 61/20 Accessories; Auxiliary operations
• CPC Class Codes: B01D 63/0222 using centrifugal forces
• CPC Class Codes: B01D 63/023 Encapsulating materials
• CPC Class Codes: B01D 63/0231 using supporting structures, e.g. filaments for weaving mats
• CPC Class Codes: B01D 63/026 Wafer type modules or flat-surface type modules
• CPC Class Codes: B01D 63/027 Twinned or braided type modules
• CPC Class Codes: B01D 63/04 comprising multiple hollow fibre assemblies
• CPC Class Codes: B01D 63/043 with separate tube sheets
• 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 1/444 by ultrafiltration or microfiltration
• CPC Class Codes: C02F 3/1273 Submerged membrane bioreactors
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage
• CPC Class Codes: Y10S 264/48 Processes of making filters

Abstract

A filtration device is provided for withdrawing permeate essentially continuously from a multicomponent aqueous substrate containing growing microorganisms in a reservoir. A vertical skein of fiber is scrubbed with coarse bubbles which emanate from a conversion baffle positioned under the skein. The substrate is aerated with fine bubbles in a size range small enough to transfer oxygen to the substrate efficiently. The baffle traps the fine bubbles and converts them to coarse bubbles which are effective to scrub the fibers. In the most preferred embodiment, the finished headers of the skein are derived from composite headers comprising a fixing lamina of resin in which the fibers are potted near their terminal ends, and a fugitive lamina of fugitive powdery material in which the terminal ends of the fibers are potted. The fugitive lamina is removed, preferably by dissolving the powder, e.g. finely divided common salt in water.

Claims

1. A process for withdrawing filtered permeate from a substrate comprising the steps of:

providing a reservoir containing non-pressurized substrate;

providing an assembly having,

an upper solid body and a lower solid body, an upper face of the lower solid body being separated from a lower face of the upper solid body by a distance;

a plurality of hollow fiber filtering membranes disposed generally vertically between the solid bodies, the ends of the membranes secured in the solid bodies, the membranes sealed in the solid bodies in a manner that prevents non-pressurized substrate from contaminating the permeate, the membranes each having a length between the solid bodies at least 1.001 times the distance but not longer than 1.05 times the distance, the membranes secured in the solid bodies such that each of the membranes may move against one or more others of the membranes;

an enclosure sealed to the upper solid body in a manner that the enclosure and the upper solid body define a cavity and prevent non-pressurized substrate from entering the cavity, the enclosure being immersible in the non-pressurized substrate;

a permeate port in communication with the cavity;

the lumen of each membrane in fluid communication with the port via the cavity;

a structure having holes through an upper part and walls extending downwards from the upper part; and

,

applying a suction to lumens of the membranes via the permeate port to withdraw permeate from the non-pressurized substrate in the reservoir;

directing a gas to flow into the structure and through the holes to provide bubbles in the non-pressurized substrate in the reservoir above the structure during the step of applying the suction; and

,

adding feed water to the reservoir so that the membranes are immersed in non-pressurized substrate in the reservoir during the step of applying the suction

wherein the gas consists essentially of air.

2. The process of claim 1 wherein the step of directing the gas is performed intermittently.

3. The process of claim 1 wherein the bubbles are provided during the step of directing the gas in an amount in a range from 0.001 scfm per membrane to about 0.03 scfm per membrane.

4. The process of claim 1 further comprising a step of withdrawing non-pressurized substrate from the reservoir during the step of applying the suction.

5. The process of claim 4 further comprising a step of withdrawing non-pressurized substrate from the reservoir during the steps of directing the gas and applying the suction.

6. The process of claim 1 wherein non-pressurized substrate is not removed from the reservoir while applying the suction.