Ultrafiltration and microfiltration module and system

• US 6,814,861 B2
• Filed: 11/04/2002
• Issued: 11/09/2004
• Est. Priority Date: 09/29/1999
• Status: Active Grant

• Current Assignee: Zenon Technology Partnership
• Original Assignee: Zenon Environmental Incorporated
• Inventors: Blair, Michael, Draesner, Andreas, Behmann, Henry, Husain, Hidayat
• Primary Examiner(s): FORTUNA, ANA M
• Application Number:
  US10/286,930
• Publication Number:
  US 20030057155A1
• Time in Patent Office: 736 Days
• Field of Search: 219/257.2, 219/650, 219/636, 219/195.1, 219/333.01, 219/136, 219/321.8
• US Class Current: 210/257.2
• CPC Class Codes: B01D 2321/04 Backflushing
• CPC Class Codes: B01D 2321/10 Use of feed
• CPC Class Codes: B01D 2321/12 Use of permeate
• CPC Class Codes: B01D 2321/168 Use of other chemical agents
• CPC Class Codes: B01D 2321/2066 Pulsated flow
• CPC Class Codes: B01D 2321/2083 By reversing the flow
• CPC Class Codes: B01D 61/145 Ultrafiltration
• CPC Class Codes: B01D 61/147 Microfiltration
• CPC Class Codes: B01D 61/18 Apparatus therefor
• CPC Class Codes: B01D 63/024 with a single potted end
• CPC Class Codes: B01D 65/02 Membrane cleaning or sterilisation ; Membrane regeneration
• CPC Class Codes: C02F 1/444 by ultrafiltration or microfiltration

Abstract

A method and apparatus of purifying feedwater to remove impurities including suspended solids therefrom, the method suitable for using in-line water pressure to permeate water through hollow fiber membranes and to backflush the membranes to remove solids collected or deposited thereon.

Claims

1. A system for purifying feedwater to remove impurities including solids therefrom, the system for use with in-line water pressure to permeate water through membranes and to remove solids collected thereon, the system comprising:

(a) a closed chamber having a first end and a second end and a first region and a second region, a feedwater entrance for connecting to a feedwater line, a permeate water exit and a concentrate water exit;

(b) membranes provided in said chamber and adapted for permeating water therethrough to purify water to provide permeate water and to reject solids under in-line water pressure to provide concentrate water in said chamber;

(c) a permeate collector for collecting said permeate water through said permeate water exit for distribution;

(d) a pressure tank in fluid connection with said permeate water collector, said pressure tank adapted for storing permeate water at in-line water pressure, said pressure tank adapted for backflushing said membranes with permeate water; and

(e) means for periodically draining concentrate water from said chamber through said concentrate water exit and lowering the pressure in said chamber below in-line water pressure, and means for backwashing said membranes with permeate water from said pressure tank to dislodge solids from said membranes for removal with said concentrate water during said draining, said means for backwashing activated by said means for draining and lowering the pressure in said chamber.

2. The system in accordance with claim 1 wherein said membranes are hollow fiber membranes disposed between said first and said second end, said membranes in fluid connection with said permeate water exit and having dead-ends potted in a first header disposed in said first region of said chamber and second ends potted in a second header disposed in said second region of said chamber, said second ends of said membranes having lumens adapted to empty permeate water into said permeate collector.

3. The system in accordance with claim 1 wherein said membranes are ultrafiltration membranes.

4. The system in accordance with claim 1 wherein said membranes are microfiltration membranes.

5. The system in accordance with claim 1 including providing means for flushing said chamber with feedwater during activation of means for draining and backflushing.

6. The system in accordance with claim 1 wherein the pressure tank is disposed below said chamber.

7. The system in accordance with claim 1 wherein said bundles of membranes are arranged substantially vertically in said chamber and said concentrate water exit is located substantially below said membranes to facilitate draining.

8. A system for purifying feedwater to remove impurities including solids therefrom, the system adapted to use in-line water pressure to permeate water through membranes and to remove solids collected thereon, the system comprising:

(a) a closed chamber having a first end and a second end, a feedwater entrance in said chamber for connecting to a feedwater line and, a permeate water exit and a concentrate water exit;

(b) bundles of hollow fiber membranes selected from ultrafiltration and microfiltration membranes provided in said chamber and disposed between said first end and said second end, said hollow fiber membranes in fluid connection with said permeate water exit and adapted for permeating water from said chamber therethrough into lumens thereof to purify water and reject solids under in-line water pressure to provide concentrate water in said chamber;

(c) a permeate water collector adapted for removal of permeate water from said lumens for re-distribution;

(d) a pressure tank in liquid communication with said permeate water collector for storing permeate water in said pressure tank at in-line water pressure, said pressure tank adapted for backwashing said membranes with permeate water; and

(e) valve means for periodically draining concentrate water from said chamber through said concentrate water exit and for lowering the pressure in said chamber below the in-line water pressure, said valve means draining and lowering the pressure in said chamber, by said means capable of

(i) activating backwashing of said membranes with permeate water from said pressure tank to dislodge solids from said membranes for removal with said concentrate water during said draining, and

(ii) activating flushing of said chamber with feedwater during said periodically draining concentrate water and backwashing.

9. An assembly for purifying feedwater to remove impurities including solids therefrom, the assembly for use with in-line water pressure to permeate water through membranes and to remove solids collected thereon, the assembly comprised of:

(a) a closed chamber having a first end and a second end, a feedwater entrance located in said first end for connecting to a feedwater line, a permeate water exit and a concentrate water exit;

(b) bundles of hollow fiber membranes provided in said chamber and disposed between said first end and said second end, said hollow fiber membranes in fluid connection with said permeate water exit and adapted for permeating water from said chamber therethrough into lumens thereof to purify water and reject solids under in-line water pressure to provide concentrate water in said chamber;

(c) a permeate collector adapted for collecting water from said lumens for distribution;

(d) a pressure tank coupled to said permeate water collector, said pressure tank adapted for storing permeate water at in-line water pressure, said pressure tank arranged for backwashing said membranes with permeate water; and

(e) valve means arranged for periodically draining concentrate water from said chamber through said concentrate water exit and lowering the water pressure in said chamber below in-line water pressure, said valve means by draining and lowering pressure in said chamber, activating backwashing of said membranes with permeate water from said diaphragm tank to dislodge solids from said membranes for removal with said concentrate water during said draining.

10. An assembly for purifying feedwater to remove impurities including solids therefrom, the assembly for use with in-line water pressure to permeate water through membranes and to remove solids collected thereon, the assembly comprised of:

(a) a closed chamber having a first end and a second end, a feedwater entrance located in said first end for connecting to a feedwater line, a permeate water exit and a concentrate water exit;

(b) bundles of hollow fiber membranes provided in said chamber and disposed between said first end and said second end, said hollow fiber membranes in fluid connection with said permeate water exit and adapted for permeating water from said chamber therethrough into lumens thereof to purify water and reject solids under in-line water pressure to provide concentrate water in said chamber;

(c) a permeate collector adapted for collecting water from said lumens for distribution;

(d) a pressure tank in fluid connection with said permeate water collector, said pressure tank adapted for storing permeate water at in-line water pressure, said pressure tank adapted for backflushing said membranes with permeate water; and

(e) a controller arranged for periodically opening and closing a concentrate water exit valve to drain concentrate water from said chamber through said concentrate water exit and to lower the pressure in said chamber below in-line water pressure, and said pressure tank activated for backwashing said membranes with permeate water by lowering the pressure in said chamber.