Immersed membrane filtration system and overflow process

• US 7,052,610 B2
• Filed: 01/21/2005
• Issued: 05/30/2006
• Est. Priority Date: 11/18/1999
• Status: Expired due to Term

• Current Assignee: Zenon Technology Partnership
• Original Assignee: Zenon Environmental Incorporated (Veolia Environnement SA)
• Inventors: Janson, Arnold, Cote, Pierre Lucien, Pedersen, Steven Kristian, Cadera, Jason, Adams, Nicholas William Harcsar
• Primary Examiner(s): FORTUNA, ANA M
• Application Number:
  US11/038,278
• Publication Number:
  US 20050121389A1
• Time in Patent Office: 494 Days
• Field of Search: 210/636, 210/650, 210/321.8, 210/321.69, 210/321.78, 210/220, 210/333.01, 210/333.1, 134/10
• US Class Current: 210/636
• CPC Class Codes: B01D 2313/06 External membrane module supporting or fixing means
• CPC Class Codes: B01D 2313/54 Modularity of membrane module elements
• CPC Class Codes: B01D 2315/06 Submerged-type; Immersion type
• CPC Class Codes: B01D 2321/185 Aeration
• 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 61/20 Accessories; Auxiliary operations
• CPC Class Codes: B01D 63/024 with a single potted end
• CPC Class Codes: B01D 63/026 Wafer type modules or flat-surface type modules
• CPC Class Codes: B01D 63/031 Two or more types of hollow fibres within one bundle or within one potting or tube-sheet
• 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 63/16 Rotary, reciprocated or vibrated modules
• CPC Class Codes: B01D 65/02 Membrane cleaning or sterilisation ; Membrane regeneration
• CPC Class Codes: B01D 65/104 Detection of leaks in membrane apparatus or modules
• CPC Class Codes: C02F 1/444 by ultrafiltration or microfiltration

Abstract

Modules of ultrafiltration or microfiltration membranes are arranged in a tank open to the atmosphere to substantially cover the cross sectional area of the tank. A filtration cycle has permeation steps and deconcentration steps. During permeation, supply of feed substantially equals feed removed and little if any aeration is used. During deconcentration, aeration with scouring bubbles is provided with one or both of backwashing and feed flushing. In feed flushing, feed water is supplied to the tank from below the modules. Excess tank water created during deconcentration flows generally upwards through the modules and out through a retentate outlet or overflow at the top of the tank.

Claims

1. A process of filtering water comprising the steps of,

a) providing one or more modules of filtering membranes immersed in water in a tank open to the atmosphere;

b) providing one or more open channels connected to a retentate outlet, the one or more open channels spanning a portion of the tank above the one or more modules;

c) permeating filtered water by (i) adding a selected volume of feed water to the tank and (ii) withdrawing substantially the selected volume of water through the one or more modules as permeate;

d) periodically stopping permeation to perform a deconcentration step, the deconcentration step further comprising at least one of (I) backwashing or (II) providing a flow of feed water into the tank from below the modules or both (I) and (II); and

,

e) flowing excess water containing retained solids out of the retentate outlet via the one or more open channels during the deconcentration step.

2. The process of claim 1 wherein the modules cover most of the horizontal cross sectional area of the tank.

3. The process of claim 1 further comprising a step of providing scouring bubbles which contact the membranes during steps (c) or (d).

4. The process of claim 1 wherein the filtering membranes are hollow fibres oriented horizontally.

5. The process of claim 1 wherein feed water is provided from above the modules during permeation.