High solids dissolved air flotation system and methods

Patent metadata

Field	Value
Publication number	US-11352275-B2
Application number	US-201916980605-A
Country	US
Kind code	B2
Filing date	Mar 13, 2019
Priority date	Mar 14, 2018
Publication date	Jun 7, 2022
Grant date	Jun 7, 2022

Abstract

A wastewater treatment system including an aeration unit, a contact tank, a dissolved air flotation unit, and a biological treatment unit is disclosed. A method of retrofitting a wastewater treatment system by providing an aeration unit and fluidly connecting the aeration unit to the wastewater treatment system is also disclosed. A method of treating wastewater including aerating wastewater with oxygen, combining the aerated wastewater with activated sludge, floating biosolids from the activated wastewater, and biologically treating the effluent is also disclosed. The method optionally includes combining the floated biosolids with the aerated wastewater and/or activated wastewater. A method of facilitating treatment of high solids content wastewater is also disclosed.

First claim

What is claimed is:

1. A wastewater treatment system comprising:
an aeration unit having a first inlet fluidly connectable to a source of a wastewater to be treated, a second inlet fluidly connectable to a source of oxygen, a third inlet, and an outlet, the aeration unit configured to aerate the wastewater with the oxygen to form a first mixed liquor;
a contact tank having a first inlet fluidly connected to the outlet of the aeration unit, a second inlet, and an outlet, the contact tank configured to treat the first mixed liquor with activated sludge to form a second 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 fluidly connected to the third inlet of the aeration unit, a second floated solids outlet fluidly connected to the second inlet of the contact tank, and an effluent outlet, the dissolved air flotation unit configured to treat the second mixed liquor with the gas to form floated solids and effluent; and
a biological treatment unit having a first inlet fluidly connected to the effluent outlet of the dissolved air flotation unit, and an outlet, the biological treatment unit configured to treat the effluent from the dissolved air flotation unit to form a third mixed liquor.

2. The system of claim 1 , further comprising:
a first metering valve positioned upstream from the first floated solids outlet and the second floated 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 floated solids to the aeration unit and the contact tank.

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

4. The system of claim 3 , wherein the solids-liquid separation unit has a third return activated sludge outlet and the aeration unit has a fourth inlet fluidly connected to the third return activated sludge outlet.

5. The system of claim 4 , further comprising:
a second metering valve positioned upstream from the first return activated sludge outlet and the third return activated sludge outlet; and
a second controller operatively connected to the second metering valve and configured to instruct the second metering valve to selectively dispense the return activated sludge to the contact tank and the aeration unit.

6. The system of claim 1 , wherein the contact tank has a third inlet fluidly connectable to the source of the wastewater to be treated.

7. The system of claim 1 , wherein the dissolved air flotation unit has a third floated solids outlet, the system further comprising an anaerobic digester having an inlet fluidly connected to the third floated solids outlet.

8. The system of claim 1 , comprising a first subsystem including the aeration unit, contact tank, and dissolved air flotation unit and a second subsystem including the biological treatment unit and the solids-liquid separation unit.

9. The system of claim 8 , wherein the aeration unit and the contact tank are included in a same treatment tank.

10. A method of treating wastewater comprising:
directing the wastewater into an aeration unit and aerating the wastewater with oxygen to form an aerated mixed liquor; directing the aerated mixed liquor into a contact tank and mixing the aerated mixed liquor 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 the aeration unit and a second portion of the floated bio solids into the contact tank; and
directing the effluent into a biological treatment unit and biologically treating the effluent to form a biologically treated mixed liquor.

11. The method of claim 10 , 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; and
directing a first portion of the activated sludge into the biological treatment unit.

12. The method of claim 11 , further comprising selectively directing a second portion of the activated sludge into the contact tank and a third portion of the activated sludge into the aeration unit.

13. The method of claim 10 , further comprising directing a second portion of the wastewater into the contact tank.

14. The method of claim 10 , comprising directing the wastewater having at least about 5% solids content into the aeration unit.

15. The method of claim 14 , comprising directing the wastewater having at least about 20% solids content into the aeration unit.

16. The method of claim 10 , wherein a minority fraction of biological oxygen demand in the wastewater introduced into the aeration unit is oxidized in the aeration unit.

17. The method of claim 16 , wherein a greater amount of biological oxygen demand in the wastewater introduced into the aeration unit is oxidized in the aeration unit than biological oxygen demand in the aerated mixed liquor is oxidized in the contact tank.

18. A method of retrofitting a wastewater treatment system comprising a contact tank, a dissolved air flotation unit, and a biological treatment unit, the method comprising:
providing an aeration unit having a first inlet fluidly connectable to a source of wastewater to be treated, a second inlet fluidly connectable to a source of oxygen, a third inlet, and an outlet, the aeration unit configured to aerate the wastewater with the oxygen to form an aerated mixed liquor;
fluidly connecting the outlet of the aeration unit to an inlet of the contact tank;
fluidly connecting the third inlet to a floated solids outlet of the dissolved air flotation unit;
fluidly connecting a first metering valve positioned downstream from the floated solids outlet; and
comprising installing a first controller operatively connected to the first metering valve and configured to instruct the first metering valve to selectively dispense the floated solids to the aeration unit and the contact tank.

19. The method of claim 18 , wherein the system further comprises a solids-liquid separation unit, the method further comprising fluidly connecting a fourth inlet of the aeration unit to a return activated sludge outlet of the solids-liquid separation unit.

20. The method of claim 19 , wherein the system further comprises a second metering valve positioned downstream from the return activated sludge outlet, the method comprising installing a second controller operatively connected to the second metering valve and configured to instruct the second metering valve to selectively dispense the return activated sludge to the aeration unit and the contact tank.

Assignees

• Evoqua Water Tech Llc

Inventors

• Erdogan Argun Olcayto
• Doyle michael l

Classifications

• Y02W10/10

  Biological treatment of water, waste water, or sewage · CPC title

• C02F3/1284

  Mixing devices · CPC title

• C02F3/30

  Aerobic and anaerobic processes · CPC title

• C02F2301/046

  Recirculation with an external loop · CPC title

• C02F2209/08

  Chemical Oxygen Demand [COD]; Biological Oxygen Demand [BOD] · CPC title