Dissolved air flotation system and methods for biological nutrient removal

Patent metadata

Field	Value
Publication number	US-11299415-B2
Application number	US-201916979855-A
Country	US
Kind code	B2
Filing date	Mar 12, 2019
Priority date	Mar 12, 2018
Publication date	Apr 12, 2022
Grant date	Apr 12, 2022

Abstract

A wastewater treatment system including a contact tank, a dissolved air flotation unit, a fermentation unit, and a biological treatment unit is disclosed. A method of retrofitting a wastewater treatment system by arranging the wastewater treatment system such that floated biosolids are fermented in an anerobic environment and fluidly connecting the biological treatment unit to receive at least a portion of the fermented solids is also disclosed. The method optionally includes providing a fermentation unit and fluidly connecting the fermentation unit to a biological treatment unit. A method of treating wastewater including combining the wastewater with activated sludge, floating biosolids from the activated wastewater, fermenting the floated biosolids, and biologically treating the effluent with the fermented solids is also disclosed. A method of facilitating delivery of soluble organic carbon to a biological treatment unit is also disclosed.

First claim

What is claimed is:

1. A wastewater treatment system comprising:
a contact tank having a first inlet fluidly connectable to a source of wastewater to be treated, and an outlet, the contact tank configured to treat the wastewater with activated sludge to form a first mixed liquor;
a dissolved air flotation unit having a first inlet fluidly connected to the outlet of the contact tank, a second inlet fluidly connected to a source of gas, a first floated solids outlet, a second floated solids outlet, and an effluent outlet, the dissolved air flotation unit configured to treat the first mixed liquor with the gas to form floated solids and an effluent;
a fermentation unit having a first inlet fluidly connected to the first floated solids outlet, a first fermented solids outlet, and a second fermented solids outlet, the fermentation unit configured to treat at least a portion of the floated solids to form fermented solids;
an anaerobic digester having a first inlet fluidly connected to the second floated solids outlet, a second inlet fluidly connected to the second fermented solids outlet, and an outlet; and
a biological treatment unit having a first inlet fluidly connected to the effluent outlet, a second inlet fluidly connected to the first fermented solids outlet, and an outlet, the biological treatment unit configured to treat the effluent with at least a portion of the fermented solids to form a second mixed liquor.

2. The system of claim 1 , wherein the contact tank has a second inlet and the biological treatment unit has a third inlet, the system further comprising:
a solids-liquid separation unit having an inlet fluidly connected to the outlet of the biological treatment unit, a solids-lean effluent outlet, a first return activated sludge outlet fluidly connected to the second inlet of the contact tank, and a second return activated sludge outlet fluidly connected to the third inlet of the biological treatment unit, the solids-liquid separation unit configured to treat solids from the second mixed liquor to form a solids-lean effluent and return activated sludge.

3. The system of claim 1 , further comprising a screen positioned between the first floated solids outlet and the first inlet of the fermentation unit, the screen configured to retain non-biological waste solids.

4. The system of claim 1 , further comprising:
a first metering valve positioned upstream from the first fermented solids outlet and the second fermented solids outlet; and
a first controller operatively connected to the first metering valve and configured to instruct the first metering valve to selectively dispense the fermented solids to the biological treatment unit and to the anaerobic digester.

5. The system of claim 1 , further comprising a screen positioned between the second floated solids outlet and the first inlet of the anaerobic digester, the screen configured to retain non-biological waste solids.

6. The system of claim 1 , wherein the fermentation unit further comprises a third fermented solids outlet and the contact tank further comprises a third inlet fluidly connected to the third fermented solids outlet.

7. The system of claim 6 , further comprising a screen positioned between the third fermented solids outlet and the third inlet of the contact tank, the screen configured to retain non-biological waste solids.

8. The system of claim 1 , wherein the contact tank comprises a second outlet and the biological treatment unit comprises:
an anaerobic region having a first inlet fluidly connected to the effluent outlet, and an outlet;
an aerated anoxic region having a first inlet fluidly connected to the second outlet of the contact tank, a second inlet fluidly connected to the outlet of the anaerobic region, and an outlet; and
an aerobic region having a first inlet fluidly connected to the outlet of the aerated anoxic region, a second inlet fluidly connected to the effluent outlet, and an outlet.

9. The system of claim 8 , wherein at least one of the anaerobic region and the aerated anoxic region has an inlet fluidly connected to the first fermented solids outlet.

10. The system of claim 9 , wherein the anaerobic region has a second inlet fluidly connected to the first fermented solids outlet and the aerated anoxic region has a third inlet fluidly connected to the first fermented solids outlet, the system further comprising:
a second metering valve positioned downstream from the first fermented solids outlet; and
and a second controller operatively connected to the second metering valve and configured to instruct the second metering valve to selectively dispense the fermented solids to the anaerobic region and to the aerated anoxic region.

11. The system of claim 8 , wherein the biological treatment unit further comprises a post-anoxic region having a first inlet fluidly connected to the outlet of the aerobic region, a second inlet fluidly connected to the first fermented solids outlet, and an outlet.

12. A method of treating wastewater comprising:
directing the wastewater into a contact tank and mixing the wastewater with an activated sludge to form an activated mixed liquor;
directing the activated mixed liquor into a dissolved air flotation unit and separating the activated mixed liquor to form a floated biosolids and an effluent;
selectively directing a first portion of the floated biosolids into a fermentation unit and a second portion of the floated biosolids into an anaerobic digester, and fermenting the first portion of the floated biosolids in the fermentation unit to form a fermented solids;
directing the effluent to a biological treatment unit; and
selectively directing a first portion of the fermented solids into the biological treatment unit and a second portion of the fermented solids into the anaerobic digester, an amount of the first portion of the fermented solids directed into the biological treatment unit being selected responsive to a determination of a required soluble chemical oxygen demand of the biological treatment unit, and biologically treating the effluent with the first portion of the fermented solids in the biological treatment unit to form a biologically treated mixed liquor.

13. The method of claim 12 , further comprising:
directing the biologically treated mixed liquor into a solids-liquid separation unit and separating the biologically treated mixed liquor to form a solids-lean effluent and the activated sludge;
directing a first portion of the activated sludge into the contact tank; and
directing a second portion of the activated sludge into the biological treatment unit.

14. The method of claim 12 , further comprising separating non-biological waste solids from at least one of the first portion of the floated biosolids and the second portion of the floated biosolids.

15. The method of claim 12 , further comprising directing a third portion of the fermented solids into the contact tank.

16. The method of claim 15 , further comprising separating non-biological waste solids from the third portion of the fermented solids.

17. The method of claim 12 , wherein the first portion of the fermented solids is selectively directed into at least one of an anaerobic region, an aerated anoxic region, and a post-anoxic region of the biological treatment unit.

18. The method of claim 12 , wherein treating the effluent with the first portion of the fermented solids comprises reducing a concentration of dissolved phosphorous in the effluent when forming the biologically treated mixed liquor.

19. A wastewater treatment sys

Assignees

• Evoqua Water Tech Llc

Inventors

• Antonneau Nathan

Classifications

• C02F11/04

  Anaerobic treatment; Production of methane by such processes · CPC title

• C02F2209/10

  Solids, e.g. total solids [TS], total suspended solids [TSS] or volatile solids [VS] · CPC title

• C02F3/1278

  Provisions for mixing or aeration of the mixed liquor · CPC title

• C02F3/28

  Anaerobic digestion processes · CPC title

• C02F2203/002

  comprising an initial buffer container · CPC title