Membrane supported biofilm process for autotrophic reduction

• US 7,175,763 B2
• Filed: 08/12/2005
• Issued: 02/13/2007
• 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
• Primary Examiner(s): Barry; Chester T.
• Application Number:
  US11/202,082
• Publication Number:
  US 20060021936A1
• Time in Patent Office: 550 Days
• Field of Search: 210/603, 210610-611, 210/615
• US Class Current: 210/603
• CPC Class Codes: C02F 3/102 Permeable membranes
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage

Abstract

A hollow gas transfer fibre is arranged in tows and potted into a module. The module may be used to treat wastewater by supplying hydrogen containing gas via the interior of the fibers to a biofilm present on an exterior surface of the fibers.

Claims

1. A method of treating wastewater comprising:

a) providing a module having fibers, the fibers each having an exterior surface exposed to the wastewater, a hollow interior, and a gas permeable wall between the interior and exterior surface; and

,

b) providing at least one of hydrogen and methane gas to the hollow interiors of the fibers, the gas penetrating the walls for feeding biofilm on the exterior surface of fibers,

wherein the amount of gas is limited to an amount that is generally less than or equal to an amount sufficient to support biomass growth at a level equal to biomass decay.

2. The method of claim 1 wherein the wastewater has 100 mg/L or less of COD.

3. The method of claim 1 further comprising maintaining the biofilm at a thickness of 1 mm or less and under endogenous respiration.

4. The method of claim 1 wherein the gas is collected from an anaerobic digester.

5. The method of claim 4 wherein the gas is converted between the anaerobic digester and the module to convert methane to hydrogen.

6. The method of claim 1 wherein the gas is taken from a source of natural gas, petroleum or propane and converted to increase its hydrogen content before applying the gas to the module.

7. The method of claim 1 wherein the module and wastewater are located in a reactor operated as a continuously stirred tank reactor.

8. The method of claim 1 wherein the module and wastewater are located in a reactor operated under plug flow conditions.

9. The method of claim 1 wherein the amount of gas is limited to limit the biomass population growing on the surface of the fibres.

10. The method of claim 1 wherein the limited biomass population is in the form of a relatively thin film on each fibre, the film on each fibre being sufficiently thin to generally avoid merging with the film of an adjacent fibre.

11. A method of controlling biomass population on fibres in a water treatment membrane reactor, the method comprising limiting the amount of feed nitrate available for consumption by the biomass so that the growth of biomass is generally equal to or less than the decay of biomass when the biomass has a population sufficient to provide a film of biomass having a thickness of 1 mm or less on the fibres of the module.

12. The method of claim 11 wherein the autotrophic denitrification load rate is maintained at a value below the ADR_EQ.