Method of combining recuperative digestion with a contact tank and dissolved air flotation

Patent metadata

Field	Value
Publication number	US-10654735-B2
Application number	US-201716309976-A
Country	US
Kind code	B2
Filing date	Jun 6, 2017
Priority date	Jun 16, 2016
Publication date	May 19, 2020
Grant date	May 19, 2020

Abstract

A wastewater treatment system includes a contact tank having a first inlet configured to receive wastewater to be treated, a second inlet configured to receive activated sludge, and an outlet, a dissolved air flotation unit having an inlet in fluid communication with the outlet of the contact tank, a biological treatment unit having a first inlet in fluid communication with an effluent outlet of the dissolved air flotation unit and an outlet, an anaerobic digester having an inlet and an outlet, a floated solids conduit providing fluid communication between the solids outlet of the dissolved air flotation unit and the inlet of the anaerobic digester, and a thickener having an inlet in fluid communication with the outlet of the anaerobic digester, a first outlet in fluid communication with the inlet of the anaerobic digester, and a second outlet.

First claim

What is claimed is:

1. A wastewater treatment system comprising:
a contact tank having a first inlet configured to receive wastewater to be treated, a second inlet configured to receive activated sludge, and an outlet, the contact tank being configured to mix the wastewater to be treated with the activated sludge to form a first mixed liquor;
a dissolved aft flotation unit having an inlet in fluid communication with the outlet of the contact tank, the dissolved air flotation unit being configured to separate suspended matter from a portion of the first mixed liquor to form a solids-lean dissolved air flotation unit effluent and floated solids, to output the floated solids through a solids outlet of the dissolved aft flotation unit, and to output the solids-lean dissolved aft flotation unit effluent through an effluent outlet of the dissolved air flotation unit;
a biological treatment unit having a first inlet in fluid communication with the effluent outlet of the dissolved air flotation unit and an outlet, the biological treatment unit being configured to biologically break down organic components of the effluent from the dissolved aft flotation unit to form a second mixed liquor;
a dissolved aft flotation unit effluent conduit extending between the effluent outlet of the dissolved aft flotation unit and the first inlet of the biological treatment unit; an anaerobic digester having an inlet and an outlet;
a floated solids conduit providing fluid communication between the solids outlet of the dissolved aft flotation unit and the inlet of the anaerobic digester;
a thickener having an inlet in fluid communication with the outlet of the anaerobic digester, a first outlet in fluid communication with the inlet of the anaerobic digester, and a second outlet, the thickener being configured to receive a portion of a digested solids stream from the outlet of the anaerobic digester, remove liquid from the portion of the digested solids stream to produce a thickened digested solids stream having an increased solids content relative to that of the portion of the digested solids stream, output the removed liquid from the second outlet, and return the thickened digested solids stream to the inlet of the anaerobic digester; and
a second thickener having an inlet in fluid communication with the outlet of the anaerobic digester downstream of the thickener, the second thickener configured to receive a second portion of the digested solids stream from the outlet of the anaerobic digester and to remove liquid from the second portion of the digested solids stream to produce a dewatered digested solids stream having an increased solids content relative to that of the second portion of the digested solids stream.

2. The system of claim 1 , wherein the thickener is a gravity belt thickener.

3. The system of claim 1 , configured to direct a majority of the digested solids stream from the outlet of the anaerobic digester to the inlet of the thickener.

4. The system of claim 1 , wherein the thickener is configured to produce the thickened digested solids stream with about twice the solids content of the digested solids stream from the outlet of the anaerobic digester.

5. The system of claim 1 , wherein the second outlet of the thickener is in fluid communication with an inlet of the contact tank.

6. The system of claim 1 , wherein the second outlet of the thickener is in fluid communication with an inlet of the biological treatment unit.

7. The system of claim 1 , wherein the second thickener includes a liquid outlet in fluid communication with an inlet of the contact tank.

8. The system of claim 1 , wherein the second thickener includes a liquid outlet in fluid communication with an inlet of the biological treatment unit.

9. The system of claim 1 , further comprising a clarifier having an inlet in fluid communication with the outlet of the biological treatment unit, an effluent outlet, and a return activated sludge outlet, the clarifier configured to output a clarified effluent through the effluent outlet and a return activated sludge though the return activated sludge outlet.

10. The system of claim 9 , further comprising a return activated sludge conduit extending between the return activated sludge outlet of the clarifier and a second inlet of the biological treatment unit.

11. The system of claim 1 , further comprising a primary clarifier having an inlet in fluid communication with a source of wastewater, a solids-lean outlet in fluid communication with the inlet of the contact tank and configured to deliver solids-lean wastewater to be treated to the inlet of the contact tank, and a solids-rich outlet in fluid communication with an inlet of a second thickener and configured to deliver a solids-rich liquid stream separated from the solids-lean wastewater to be treated to the inlet of the second thickener.

12. The system of claim 11 , wherein the second thickener includes a solids-rich outlet configured to deliver a thickened solid-rich liquid stream to an inlet of the anaerobic digester and a solids-lean outlet configured to deliver liquid separated from the solid-rich liquid stream to a third inlet of the contact tank.

13. A method of treating wastewater comprising:
introducing the wastewater into a contact tank including an activated sludge;
mixing the wastewater with activated sludge in the contact tank to form a first mixed liquor;
directing the first mixed liquor to a dissolved air flotation unit;
separating the first mixed liquor in the dissolved air flotation unit to form a solids-lean dissolved air flotation unit effluent and floated solids;
directing the solids-lean dissolved air flotation unit effluent to a biological treatment unit;
biologically treating the solids-lean dissolved air flotation unit effluent in the biological treatment unit to form a biologically treated mixed liquor;
directing the floated solids to an anaerobic digester;
biologically treating the floated solids in the anaerobic digester to form digested solids;
directing a portion of the digested solids to a thickener;
separating liquid from the digested solids in the thickener to form thickened digested solids;
recycling the thickened digested solids to the anaerobic digester; and
directing a second portion of the digested solids to a second thickener in fluid communication downstream of the anaerobic digester and thickener.

14. The method of claim 13 , further comprising directing the liquid separated from the digested solids in the thickener to the contact tank.

15. The method of claim 13 , further comprising directing the liquid separated from the digested solids in the thickener to the biological treatment unit.

16. The method of claim 13 , wherein directing the portion of the digested solids to the thickener comprises directing a majority of the digested solids formed in the anaerobic digester to the thickener.

17. The method of claim 13 , wherein separating liquid from the digested solids in the thickener comprises increasing a solids content of the digested solids by about two times in the thickener to form the thickened digested solids.

18. The method of claim 13 , further comprising dewatering the second portion of the digested solids in the second thickener.

19. The method of claim 18 , further comprising directing liquid separated from the second portion of the digested solids in the second thickener to the contact tank.

20. The method of claim 18 , further comprising directing liquid separated from the second portion of the digested soli

Assignees

• Evoqua Water Tech Llc

Inventors

• Smith George W

Classifications

• C02F3/302

  Nitrification and denitrification treatment (C02F3/308 takes precedence) · CPC title

• C02F1/5245

  using basic salts, e.g. of aluminium and iron · CPC title

• C02F3/121

  Multistep treatment · CPC title

• C02F11/04

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

• C02F1/24

  by flotation (C02F1/465 takes precedence) · CPC title