Method and apparatus for treating wastewater using membrane filters

• US 20030159988A1
• Filed: 02/11/2003
• Published: 08/28/2003
• Est. Priority Date: 07/27/2000
• Status: Active Grant

• Current Assignee: CH2M Hill Incorporated (CH2M Hill Companies Limited)
• Original Assignee: CH2M Hill Incorporated (CH2M Hill Companies Limited)
• Inventors: Daigger, Glen T., Murthy, Sudhir N., Wollmann, Albert M., Fleischer, Edwin J., Broderick, Thomas A.
• Granted Patent: US 6,863,818 B2
• Time in Patent Office: Days
• US Class Current: 210/605
• CPC Class Codes: C02F 1/283 using coal, charred products, or inorganic mixtures containing them
• CPC Class Codes: C02F 2209/22 O2
• CPC Class Codes: C02F 3/006 Regulation methods for biological treatment
• CPC Class Codes: C02F 3/12 Activated sludge processes
• CPC Class Codes: C02F 3/121 Multistep treatment
• CPC Class Codes: C02F 3/1226 comprising an absorbent material suspended in the mixed liquor
• CPC Class Codes: C02F 3/1273 Submerged membrane bioreactors
• CPC Class Codes: C02F 3/30 Aerobic and anaerobic processes
• CPC Class Codes: C02F 3/308 Biological phosphorus removal
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage

Abstract

An apparatus using activated sludge for the removal of biological nutrients from a wastewater includes a bioreactor for containing a mixture of wastewater under treatment and activated sludge. The bioreactor is divided into a plurality of serially connected treatment zones and includes a wastewater inlet, a downstream aerobic zone and an upstream aerobic zone between the wastewater inlet and the downstream aerobic zone, the upstream and downstream aerobic zones being separated by an anoxic zone. A membrane filter is provided in the downstream aerobic zone so that it functions as an immersed membrane filter with a bioreactor containing an operative volume of wastewater and activated sludge. The immersed membrane filter filters treated water flowing from the bioreactor through a first outlet. An aerator is operative associated with the membrane filter for purging solids from the membrane filter. A second outlet in the downstream aerobic zone is connected to an inlet in the upstream aerobic zone for recycling activated sludge charged with oxygen from the downstream aerobic zone to the upstream aerobic zone.

A method for removal of nutrients from a wastewater includes providing a wastewater to an inlet of a serial, multi-zone, activated sludge bioreactor containing an activated sludge. The bioreactor has a downstream aerobic zone from which water is removed and an upstream aerobic zone between the wastewater inlet and the downstream aerobic zone, the upstream and downstream aerobic zones being separated by an anoxic zone. Treated water is filtered from the activated sludge in the downstream aerobic zone through an immersed membrane filter. Solids are purged from the immersed membrane filter with an oxygen containing gas and return activated sludge charged with oxygen is recycled from the downstream to the upstream aerobic zone or to an upstream deaeriation zone.

Claims

1. A method for removal of biological nutrients from a wastewater, comprising:

providing wastewater to an inlet of a serial multizone activated sludge bioreactor containing activated sludge, the bioreactor having a downstream aerobic zone from which treated water is removed and an upstream aerobic zone between the wastewater inlet and the downstream aerobic zone, the upstream and downstream aerobic zones being separated by an anoxic zone;

filtering treated water from the activated sludge in the downstream aerobic zone through an immersed membrane filter;

purging solids from the immersed membrane filter with an oxygen containing purge gas; and

recycling return activated sludge charged with oxygen associated with the oxygen containing purge gas from the downstream aerobic zone to the upstream aerobic zone.

2. The method of claim 1 further comprising:

feeding treated water from the immersed membrane filter to a treatment tank inlet;

adding powdered activated carbon (PAC) to the treatment tank near the treatment tank inlet;

flowing the treated water and PAC along a treatment path within the treatment tank; and

filtering the treated water from the PAC through an immersed membrane filter.

3. The method of claim 2 further comprising maintaining in the treatment tank a population of micoorganisms for metabolizing dissolved organic material in the treated water.

4. The method of claim 2 further comprising monitoring the concentration of dissolved organic material in the treated water fed into the treatment tank inlet and varying the amount of PAC added to the treatment tank as a function of the concentration of dissolved organic material in the treated water.

5. The method of claim 1 further comprising continuously recycling the return activated sludge charged with oxygen associated with the oxygen containing purge gas from the downstream aerobic zone to the upstream aerobic zone.

6. The method of claim 1 further comprising continuously purging solids from the immersed membrane filter.

7. An apparatus utilizing activated sludge for the removal of biological nutrients from a wastewater, comprising:

a bioreactor for containing a mixture of wastewater under treatment and activated sludge, the bioreactor being divided into a plurality of serially connected treatment zones, and having a wastewater inlet, a downstream aerobic zone and an upstream aerobic zone between the wastewater inlet and the downstream aerobic zone, the upstream and downstream aerobic zones being separated by an anoxic zone;

a membrane filter in the downstream aerobic zone, the membrane filter being situated in the downstream aerobic zone so that it functions as an immersed membrane filter with the bioreactor containing an operative volume of wastewater and activated sludge, the immersed membrane filter filtering treated water flowing from the bioreactor through a first outlet;

an aerator operatively associated with the membrane filter for purging solids from the membrane filter with an oxygen containing purge gas; and

a second outlet in the downstream aerobic zone connected to an inlet in the upstream aerobic zone for recycling return activated sludge charged with oxygen associated with the oxygen containing purge gas from the downstream aerobic zone to the upstream aerobic zone.

8. The apparatus of claim 7 further comprising:

a treatment tank having an inlet coupled to the first outlet for receiving treated water and a downstream outlet;

a powdered activated carbon (PAC) supply operatively associated with the treatment tank for providing PAC to the treatment tank near the treatment tank inlet; and

a membrane filter operatively associated with the downstream outlet, the membrane filter being situated so that if functions as an immersed membrane filter with the treatment tank containing an operative volume of treated water.

9. The apparatus of claim 8 further comprising monitoring means for monitoring a concentration of dissolved organics in the treated water flowing into the receiving tank inlet, the monitoring means being operatively associated with the PAC supply to vary the amount of PAC provided to the treatment tank as a function of the concentration of dissolved organics in the treated water.

10. The apparatus of claim 7 wherein the second outlet continuously recycles return activated sludge charged with oxygen associated with the oxygen containing purge gas from the downstream aerobic zone to the upstream aerobic zone.

11. A method for removal of biological nutrients from a wastewater, comprising:

providing wastewater to an inlet of a serial multizone activated sludge bioreactor containing activated sludge, the bioreactor having a downstream aerobic zone from which treated water is removed and upstream aerobic zone between the wastewater inlet and the downstream aerobic zone, the upstream and downstream aerobic zones being separated by an anoxic zone;

filtering treated water from the activated sludge in the downstream aerobic zone through an immersed membrane filter;

purging solids from the immersed membrane filter with an oxygen containing purge gas; and

recycling return activated sludge charged with oxygen associated with the oxygen containing purge gas from the downstream aerobic zone to a deaeration zone upstream of the bioreactor inlet.

12. The method of claim 11 further comprising continuously purging solids from the immersed membrane filter.

13. The method of claim 11 further comprising:

feeding treated water from the immersed membrane filter to a treatment tank inlet;

adding powdered activated carbon (PAC) to the treatment tank near the treatment tank inlet;

flowing the treated water and PAC along a treatment path within the treatment tank; and

filtering the treated water from the PAC through an immersed membrane filter.

14. The method of claim 13 further comprising maintaining in the treatment tank a population of micoorganisms for metabolizing dissolved organic material in the treated water.

15. The method of claim 13 further comprising monitoring the concentration of dissolved organic material in the treated water fed into the treatment tank inlet and varying the amount of PAC added to the treatment tank as a function of the concentration of dissolved organic material in the treated water.

16. The method of claim 11 further comprising continuously recycling the return activated sludge charged with oxygen associated with the oxygen containing purge gas from the downstream aerobic zone to the upstream aerobic zone.