Supported biofilm apparatus and process

• US 7,303,676 B2
• Filed: 07/22/2004
• Issued: 12/04/2007
• Est. Priority Date: 02/13/2003
• Status: Active Grant

• Current Assignee: Zenon Technology Partnership
• Original Assignee: Zenon Technology Partnership
• Inventors: Cote, Pierre Lucien, Behmann, Henry, Husain, Hidayat, Towe, Ian Glenn, Pottinger, Ian Alexander
• Primary Examiner(s): Barry; Chester T.
• Application Number:
  US10/896,086
• Publication Number:
  US 20050051481A1
• Time in Patent Office: 1,230 Days
• Field of Search: 210/615, 210/619
• US Class Current: 210/615
• CPC Class Codes: B01D 2315/06 Submerged-type; Immersion type
• 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 63/0232 using hollow fibers mats as precursor, e.g. wound or pleated mats
• CPC Class Codes: B01D 63/027 Twinned or braided type modules
• CPC Class Codes: B01D 69/084 Undulated fibres
• CPC Class Codes: C02F 3/006 Regulation methods for biological treatment
• CPC Class Codes: C02F 3/102 Permeable membranes
• CPC Class Codes: C02F 3/1273 Submerged membrane bioreactors
• CPC Class Codes: C02F 3/301 Aerobic and anaerobic treatment in the same reactor
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage

Abstract

A membrane supported biofilm reactor uses modules having fine, hollow fibres, for example, made from melt spun thermoplastic polymers treated after spinning to increase their permeability to oxygen, used, for example, in tows or formed into a fabric. In one module, one or more sheets of the fabric are potted into a module to enable oxygen containing gas to be supplied to the lumens of the hollow fibres. Various reactors and processes, for example to treat wastewater, using such modules are described. Mechanical, chemical and biological methods, for example endogenous respiration, are used to control the thickness of the biofilm.

Claims

1. A process for treating a liquid comprising the steps of:

a) contacting an apparatus having a port in communication with one or more inner surfaces of a gas permeable biofilm support medium with the liquid; and

,

b) providing a gas to the port of the apparatus, the gas permeating to outer surface(s) of the medium to support a biofilm growing on the outer surface(s)

wherein the biofilm support medium comprises a membrane with openings of up to about 40 Angstroms in size, and

wherein the biofilm is maintained in a state of generally endogenous growth.

2. The process of claim 1 wherein the biofilm is maintained in a state of generally endogenous growth by providing a F/M ratio of 0.09 (kgCODt/kgMLSS)/d or less.

3. The process of claim 1 wherein the biofilm is maintained in a state of generally endogenous growth by providing the gas to the port at a rate which limits a supply of oxygen to the biofilm.

4. The process of claim 3 further comprising providing feed the liquid at a F/M ratio of 0.09 (kgCODt/kgMLSS)/d or more.

5. The process of claim 3 further comprising the steps of providing the liquid at a F/M ratio of greater than 0.09 (kgCODt/kgMLSS)/d to the biofilm to produce an effluent and flowing the effluent at a F/M ratio of less than 0.09 (kgCODt/kgMLSS)/d to a second bioflim maintained in a state of generally endogenous respiration.

6. The process of claim 1 further comprising providing bubbles in the liquid.

7. A process for treating wastewater comprising steps of:

(a) contacting wastewater comprising COD against a first surface of a gas permeable but liquid water impermeable membrane;

(b) providing an oxygen bearing gas to a second surface of the membrane such that oxygen passes to the first surface of the membrane; and

,

(c) limiting the F/M ratio of the wastewater or the supply of oxygen bearing gas so as to support a biofllm on the first surface of the membrane in a state of generally endogenous respiration at a thickness of less than 2 mm.

8. The process of claim 7 wherein the bioflim is maintained at a thickness of 1 mm or less.

9. The process of claim 7 further comprising mixing the wastewater.

10. The process of claim 9 wherein the wastewater is mixed by introducing bubbles into the wastewater.