Cyclic aeration system for submerged membrane modules

• US 6,245,239 B1
• Filed: 01/19/2000
• Issued: 06/12/2001
• Est. Priority Date: 10/09/1998
• Status: Expired due to Term

• Current Assignee: Zenon Technology Partnership
• Original Assignee: Zenon Environmental Incorporated
• Inventors: Janson, Arnold, Singh, Manwinder, Cote, Pierre, Rabie, Hamid
• Primary Examiner(s): Bushey, C. Scott
• Application Number:
  US09/488,359
• Time in Patent Office: 510 Days
• Field of Search: 261/23.1, 261/28, 261/43, 261/59, 261/64.1, 261/124, 210/636, 210/641, 210/644, 210/649, 210/650, 210/651, 210/652, 210/138, 210/142, 210/321.75, 210/321.78, 210/321.79, 210/321.84, 210/321.88
• US Class Current: 210/636
• CPC Class Codes: B01D 2313/26 Specific gas distributors or gas intakes
• CPC Class Codes: B01D 2315/06 Submerged-type; Immersion type
• CPC Class Codes: B01D 2321/04 Backflushing
• CPC Class Codes: B01D 2321/18 Use of gases
• CPC Class Codes: B01D 2321/185 Aeration
• CPC Class Codes: B01D 61/18 Apparatus therefor
• CPC Class Codes: B01D 63/02 Hollow fibre modules
• 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 63/033 Specific distribution of fibres within one potting or tube-sheet
• 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: B01F 23/23105 Arrangement or manipulation of the gas bubbling devices
• CPC Class Codes: B01F 23/231231 the outlets being in the form of perforations
• CPC Class Codes: B01F 23/231242 in the form of slits or cut-out openings
• CPC Class Codes: B01F 23/231265 being tubes, tubular elements, cylindrical elements or set of tubes
• CPC Class Codes: B01F 23/2319 Methods of introducing gases into liquid media
• CPC Class Codes: B01F 33/4062 with means for modifying the gas pressure or for supplying gas at different pressures or in different volumes at different parts of the bottom
• CPC Class Codes: C02F 1/444 by ultrafiltration or microfiltration
• CPC Class Codes: C02F 1/74 : with air aeration of stretches of water C02F7/00
• CPC Class Codes: C02F 2209/40 : Liquid flow rate
• CPC Class Codes: C02F 2209/44 : Time
• CPC Class Codes: C02F 3/1273 : Submerged membrane bioreactors
• CPC Class Codes: C02F 3/201 : Perforated, resilient plastic diffusers, e.g. membranes, sheets, foils, tubes, hoses
• CPC Class Codes: Y02W 10/10 : Biological treatment of water, waste water, or sewage

Abstract

An aeration system for a submerged membrane module has a set of aerators connected to an air blower, valves and a controller adapted to alternately provide a higher rate or air flow and a lower rate of air flow in repeated cycles. In an embodiment, the air blower, valves and controller, simultaneously provide the alternating air flow to two or more sets of aerators such that the total air flow is constant, allowing the blower to be operated at a constant speed. In another embodiment, the repeated cycles are of short duration. Transient flow conditions result in the tank water which helps avoid dead spaces and assists in agitating the membranes.

Claims

1. A method of aerating a plurality of membrane modules immersed in water in a tank comprising the steps of:

providing a flow of air to aerators below the membrane modules, the flow of air alternating between a higher flow rate of flow and a lower flow rate of flow, the lower flow rate being less than one half of the higher flow rate, in repeated cycles of are greater than about 10 seconds and less than about 120 seconds in duration to produce transient now conditions in the water in the tank and accelerate or decelerate the water in the tank for much of the cycle so that the water in the tank is rarely in a steady state.

2. The method of claim 1 wherein the repeated cycles are between about 20 seconds and about 60 seconds in duration.

3. The invention of claim 2 wherein the lower flow rate is an air off condition.

4. The invention of claim 3 wherein the higher flow rate corresponds to a superficial velocity in relation to the aerators receiving the flow of air of between 0.013 m/s and 0.15 m/s.

5. A method of aerating a plurality of immersed membrane modules comprising:

(a) providing a first set of aerators below the membrane modules interspersed in a horizontal plane with a second set of aerators below the membrane modules such that a plurality of aerators in the first set of aerators are each adjucent to aerators in the second set of aerators;

(b) providing an initial air flow at an initial flow rate;

(c) splitting and allocating the initial air flow such that for a first period of time the first set of aerators receives air at a higher flow rate while the second set of aerators receives air at a lower flow rate and that for a second period of time the first set of aerators receives air at a lower flow rate while the second set of aerators receives air at a higher flow rate in repeated cycles of between about 10 seconds and about 120 seconds in duration.

6. The invention of claim 5 wherein the cycles are between 20 and 40 seconds in duration.

7. The invention of claim 5 wherein the lower flow rate is an air off condition.

8. The aeration system of claim 7 wherein the higher flow rate of gas flow corresponds to a superficial velocity between 0.013 m/s and 0.15 m/s.