Bioreactor with suspended biomass and membrane supported biofilm

• US 8,986,540 B2
• Filed: 09/12/2013
• Issued: 03/24/2015
• Est. Priority Date: 04/20/2007
• Status: Active Grant

• Current Assignee: BL Technologies Inc. (Ashland Global Holdings, Inc.)
• Original Assignee: Zenon Technology Partnership
• Inventors: Husain, Hidayat, Mazzaferro, Rocco, Liu, Minggang, Wong, Richard, Lossing, Heather, Fan, Fengshen, Hong, Youngseck, Bayly, Reid
• Primary Examiner(s): BARRY, CHESTER T
• Application Number:
  US14/024,823
• Publication Number:
  US 20140008280A1
• Time in Patent Office: 558 Days
• Field of Search: 210/622, 210150-151, 210/197, 210/220
• US Class Current: 210/150
• CPC Class Codes: B01D 2313/143 on the feed side
• CPC Class Codes: B01D 2313/21 Specific headers, end caps
• CPC Class Codes: B01D 2313/23 Specific membrane protectors, e.g. sleeves or screens
• CPC Class Codes: B01D 2315/06 Submerged-type; Immersion type
• CPC Class Codes: B01D 63/043 with separate tube sheets
• CPC Class Codes: B01D 67/0097 Storing or preservation
• CPC Class Codes: C02F 2203/006 details of construction, e.g. specially adapted seals, modules, connections
• CPC Class Codes: C02F 3/102 Permeable membranes
• CPC Class Codes: C02F 3/208 Membrane aeration C02F3/201 takes precedence
• CPC Class Codes: C02F 3/2806 Anaerobic processes using solid supports for microorganisms
• CPC Class Codes: C02F 3/302 Nitrification and denitrification treatment C02F3/308 takes precedence
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage

Abstract

A membrane supported biofilm apparatus has a plurality of hollow fiber gas permeable membranes in a tank containing water to be treated. A biofilm supported on the membranes occupies between about 40% and 80% of the volume of water to be treated in a reactor. Wastewater treatment processes are described. A process to denitrify water or treat oxidized contaminants comprises introducing hydrogen into an inner volume of the membranes to grow autotrophic organisms in the biofilm near the membrane and heterotrophic organism near the water. Another process is operated as a biomass concentration of at least 10 g/L and up to about 40 g/L to maintain a biofilm having a surface area of over 1000 square meters per cubic meter of tank volume. A hybrid process has suspended biomass and a membrane supported biofilm.

Claims

1. A bioreactor having,

a tank for holding water to be treated containing both a suspended biomass and a membrane-supported biofilm;

a solids separation device downstream of the tank; and

,

a recycle of separated solids from the solids separation device to the tank,

wherein the recycle passes through an anoxic stage before returning to the tank.

2. The bioreactor of claim 1 having a mixer to kept the suspended biomass in suspension.

3. The bioreactor of claim 1 comprising a module located in the tank, the module having a plurality of gas permeable hollow fiber membranes collected at a lower end in a header and having upper ends held or floated near a water surface of the tank with the header on or near the bottom of the tank wherein the hollow fiber membranes support the membrane-supported biofilm.

4. The bioreactor of claim 3 wherein the membranes are impermeable to bulk or advective water flow and have an outside diameter of about 200 microns or less and a length within the range of about 3-10 meters.

5. The bioreactor of claim 3, wherein the hollow fiber membranes are placed in the tank at a dry fiber packing density in the range of about 0.5% to 4%.

6. The bioreactor of claim 3, wherein the hollow fiber membranes support a biofilm occupying about 40% or more of the volume of the tank.

7. The bioreactor of claim 3 comprising a spreader near the header to horizontally space some of the plurality of hollow fiber membranes from others of the plurality of hollow fiber membranes.

8. The bioreactor of claim 3 wherein the header is attached to an air supply manifold on or near the bottom of the tank.

9. The bioreactor of claim 3 further comprising a mixer and a solids removal port on or near the bottom of the tank.

10. The bioreactor of claim 3, wherein the hollow fiber membranes support a biofilm occupying about 80% or less of the volume of the tank.

11. The bioreactor of claim 3 wherein the tank comprises channels at a feed end of the tank for feed dispersal.