System and method for treating wastewater and resulting sludge

Patent metadata

Field	Value
Publication number	US-9758416-B2
Application number	US-201313862805-A
Country	US
Kind code	B2
Filing date	Apr 15, 2013
Priority date	Apr 15, 2013
Publication date	Sep 12, 2017
Grant date	Sep 12, 2017

Abstract

A wastewater treatment process that produces primary sludge and biological sludge. The system and process hydrolyzes the biological sludge in a hydrolysis reactor. The primary sludge is directed to a pasteurization unit and pasteurized. Thereafter, the hydrolyzed biological sludge and the pasteurized primary sludge are directed to an anaerobic digester where the combined sludges are subjected to anaerobic digestion.

First claim

What is claimed is:

1. A method of treating wastewater and resulting sludge comprising:
subjecting the wastewater to a primary treatment and producing primary sludge and a primary effluent;
subjecting the wastewater to primary treatment including directing the wastewater into a primary treatment system including a primary settling tank and settling the primary sludge in the primary settling tank and wherein the primary settling tank produces the primary effluent;
thickening the primary sludge in a primary sludge thickener;
directing the primary effluent to a biological treatment system and biologically treating the primary effluent to produce biological sludge;
after thickening the primary sludge, directing the primary sludge to a pasteurization unit and pasteurizing the primary sludge;
directing the biological sludge to a thermal hydrolysis reactor and hydrolyzing the biological sludge;
directing the pasteurized sludge and the hydrolyzed sludge to an anaerobic digester; and
anaerobically digesting the pasteurized primary sludge and the hydrolyzed biological sludge in the anaerobic digester.

2. The method of claim 1 including transferring heat from the hydrolyzed biological sludge to the primary sludge before the primary sludge enters the pasteurization unit, thereby cooling the hydrolyzed biological sludge and heating the primary sludge.

3. The method of claim 2 including directing the hydrolyzed biological sludge through a first heat exchanger downstream from the hydrolysis reactor and directing the primary sludge through a second heat exchanger upstream of the pasteurization unit; circulating a heat transfer medium through the first and second heat exchanger such that heat associated with the hydrolyzed biological sludge is transferred to the primary sludge.

4. The method of claim 3 including cooling the heat transfer medium when the ratio of primary sludge to biological sludge falls below a selected value, and heating the heat transfer medium when the ratio of the primary sludge to the biological sludge is above selected value.

5. The method of claim 3 wherein the heat transfer medium passes through at least two additional heat exchangers, a third heat exchanger for cooling the heat transfer medium and a fourth heat exchanger for heating the heat transfer medium.

6. The method of claim 5 wherein the third cooling heat exchanger is air cooled and wherein the fourth heating heat exchanger is heated by a boiler.

7. The method of claim 3 including maintaining the heat transfer medium under pressure to generally prevent the heat transfer medium from boiling.

8. The method of claim 2 including transferring heat from the pasteurized primary sludge to the primary sludge before the primary sludge enters the pasteurization unit.

9. The method of claim 1 including combining the hydrolyzed biological sludge with the pasteurized primary sludge; and directing the combined hydrolyzed biological sludge and pasteurized primary sludge into an anaerobic digester.

10. The method of claim 1 including dewatering the biological sludge before directing the biological sludge into the hydrolysis reactor.

11. The method of claim 1 wherein substantially all the thermal energy required to heat the pasteurized sludge to a pasteurization temperature is provided by transferring heat from the hydrolyzed biological sludge to the primary sludge, and by transferring heat from the pasteurized primary sludge to the primary sludge before the primary sludge enters the pasteurization unit.

12. The method of claim 1 including transferring sufficient heat from the hydrolyzed biological sludge to the primary sludge to raise the temperature of the primary sludge at least 20° C. prior to entering the pasteurization unit.

13. The method of claim 1 including raising the temperature of the primary sludge by transferring heat from the pasteurized primary sludge to the primary sludge before entering the pasteurization unit; and also raising the temperature of the primary sludge by transferring heat from the hydrolyzed biological sludge to the primary sludge before the primary sludge enters the pasteurization unit.

14. The method of claim 13 wherein raising the temperature of the primary sludge includes first transferring heat from the pasteurized primary sludge to the primary sludge and thereafter transferring heat from the hydrolyzed biological sludge to the primary sludge before the primary sludge enters the pasteurization unit.

15. The method of claim 1 including multiple cooling processes for cooling the hydrolyzed biological sludge before reaching the anaerobic digester, the multiple cooling processes including:
i. cooling the hydrolyzed biological sludge by transferring heat therefrom to the primary sludge;
ii. cooling the hydrolyzed biological sludge by transferring heat therefrom to a steam generator feedwater; and
iii. cooling the hydrolyzed biological sludge by transferring heat therefrom to a treated waste stream.

16. The method of claim 1 including processing the biological sludge such that the dry solids content of the hydrolyzed sludge exceeds the dry solids content of the pasteurized sludge, expressed on a percentage weight basis.

17. The method of claim 1 wherein the wastewater comprises a single stream of wastewater and wherein the single stream of wastewater is first subjected to primary treatment which produces the primary sludge and thereafter subjected to biological treatment downstream of the primary treatment which produces the biological sludge, and wherein both the primary sludge and biological sludge are derived from the single stream of wastewater.

18. The method of claim 17 including:
dewatering the biological sludge before directing the biological sludge into the hydrolysis reactor;
transferring heat from the hydrolyzed biological sludge to the primary sludge before the primary sludge enters the pasteurization unit, thereby cooling the hydrolyzed biological sludge and heating the primary sludge;
directing the hydrolyzed biological sludge through a first heat exchanger downstream from the hydrolysis reactor and directing the primary sludge through a second heat exchanger upstream of the pasteurization unit; circulating a heat transfer medium through the first and second heat exchanger such that heat associated with the hydrolyzed biological sludge is transferred to the primary sludge;
cooling the heat transfer medium when the ratio of primary sludge to biological sludge falls below a selected value, and heating the heat transfer medium when the ratio of the primary sludge to the biological sludge is above a selected value;
wherein the heat transfer medium passes through at least two additional heat exchangers, a third heat exchanger for cooling the heat transfer medium and a fourth heat exchanger for heating the heat transfer medium; and
wherein the third cooling heat exchanger is air cooled and wherein the fourth heating heat exchanger is heated by a boiler.

19. The method of claim 1 further including directing a steam generator feedwater to a water treatment unit and removing scaling or fouling species from the steam generator feedwater; thereafter directing the feedwater and hydrolyzed sludge to a heat exchanger and cooling the hydrolyzed biological sludge by transferring heat from the hydrolyzed biological sludge to the steam generator feedwater; and thereafter directing the steam generator feedwater to a steam generator and generating steam and utilizing the steam generated by the steam generator in hydrolyzing the biologic

Assignees

• Veolia Water Solutions & Tech
• Veolia Water Solutios & Tech Support

Inventors

• Dimassimo Richard W
• Hojsgaard Soren J

Classifications

• C02F2303/24

  Separation of coarse particles, e.g. by using sieves or screens · CPC title

• C02F2303/06

  Sludge reduction, e.g. by lysis · CPC title

• C02F11/18

  by thermal conditioning (by pyrolysis C02F11/10) · CPC title

• C02F11/185

  by pasteurisation · CPC title

• C02F11/04 Primary

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