System and method for treating wastewater and resulting primary and biological sludge

Patent metadata

Field	Value
Publication number	US-10370277-B2
Application number	US-201615058559-A
Country	US
Kind code	B2
Filing date	Mar 2, 2016
Priority date	Mar 2, 2015
Publication date	Aug 6, 2019
Grant date	Aug 6, 2019

Abstract

A method of treating primary sludge and activated sludge produced by a wastewater system is disclosed. A portion of the activated sludge is wasted to form biological sludge. The biological sludge is thermally hydrolyzed. The method entails cooling the thermally hydrolyzed biological sludge by mixing primary sludge with the thermally hydrolyzed biological sludge. Thereafter, the combined sludge is directed through a pasteurization process and then to an anaerobic digester which performs anaerobic digestion of the combined sludge.

First claim

What is claimed is:

1. A method of treating wastewater and resulting sludge comprising:
subjecting the wastewater to primary treatment and producing primary sludge;
after subjecting the wastewater to the primary treatment, subjecting the wastewater to biological treatment and producing biological sludge;
directing the biological sludge to a thermal hydrolysis unit and subjecting the biological sludge to a thermal hydrolysis process and producing thermally hydrolyzed biological sludge;
mixing the primary sludge and thermally hydrolyzed biological sludge in a pressurized structure at a pressure greater than atmospheric pressure to form a sludge mixture;
cooling the thermally hydrolyzed biological sludge in the pressurized structure by transferring sensible heat from the thermally hydrolyzed biological sludge to the primary sludge;
transferring the sludge mixture of primary sludge and thermally hydrolyzed biological sludge from the pressurized structure to a pasteurization unit and subjecting the sludge mixture to a pasteurization process; and
after pasteurizing the sludge mixture, transferring the sludge mixture from the pasteurization unit to an anaerobic digester and subjecting the sludge mixture to anaerobic digestion.

2. The method of claim 1 including reducing the temperature of the thermally hydrolyzed biological sludge by at least 80° C. by transferring sensible heat from the thermally hydrolyzed biological sludge to the primary sludge prior to the sludge mixture reaching the pasteurization unit.

3. The method of claim 1 wherein the pressurized structure includes a pressurized line leading from the thermal hydrolysis unit and wherein there are no heat exchangers engaged with the pressurized line; and the method includes transferring the thermally hydrolyzed biological sludge from the thermal hydrolysis unit through the pressurized line; and feeding the primary sludge into the pressurized line where the primary sludge and thermally hydrolyzed biological sludge are mixed and wherein substantially all cooling of the thermally hydrolyzed biological sludge is achieved by transferring the sensible heat from the thermally hydrolyzed biological sludge to the primary sludge without the aid of heat exchangers engaged with the pressurized line.

4. The method of claim 1 including moving the thermally hydrolyzed biological sludge from the thermal hydrolysis unit into and through the pressurized structure that is operatively connected to a pressure-maintaining pump that is disposed downstream of the thermal hydrolysis unit and upstream from the pasteurization unit; wherein the pressure-maintaining pump maintains a pressure greater than atmospheric pressure in the pressurized structure between the thermal hydrolysis unit and the pressure-maintaining pump; and the method includes feeding the primary sludge into the pressurized structure at a point between the thermal hydrolysis unit and the pressure-maintaining pump and mixing the thermally hydrolyzed biological sludge with the primary sludge in the pressurized structure.

5. The method of claim 4 wherein neither the thermally hydrolyzed biological sludge nor the sludge mixture is cooled by heat exchangers upstream of the pasteurization unit.

6. The method of claim 1 wherein subjecting the wastewater to primary and biological treatment produces a treated effluent and wherein the method includes mixing at least a portion of the treated effluent with the thermally hydrolyzed biological sludge or sludge mixture.

7. The method of claim 1 further including:
subjecting the wastewater to the primary and biological treatment produces a treated effluent and wherein the method includes mixing at least a portion of the treated effluent with the thermally hydrolyzed biological sludge or sludge mixture;
reducing the temperature of the thermally hydrolyzed biological sludge by at least 80° C. by transferring the sensible heat from the thermally hydrolyzed the sludge to the primary sludge prior to the sludge mixture reaching the pasteurization unit;
wherein the pressurized structure includes a pressurized line leading from the thermal hydrolysis unit and wherein there are no heat exchangers engaged with the pressurized line; and the method includes transferring the thermally hydrolyzed biological sludge from the thermal hydrolysis unit through the pressurized line; and feeding the primary sludge into the pressurized line where the primary sludge and thermally hydrolyzed biological sludge are mixed and wherein substantially all cooling of the thermally hydrolyzed biological sludge is achieved by transferring the sensible heat from the thermally hydrolyzed biological sludge to the primary sludge without the aid of heat exchangers engaged with the pressurized line;
moving the thermally hydrolyzed biological sludge from the thermal hydrolysis unit into and through the pressurized structure that is operatively connected to a pressure-maintaining pump that is disposed downstream of the thermal hydrolysis unit and upstream from the pasteurization unit; wherein the pressure-maintaining pump maintains a pressure greater than atmospheric pressure in the pressurized structure between the thermal hydrolysis unit and the pump; and the method includes feeding the primary sludge into the pressurized structure at a point between the thermal hydrolysis unit and the pressure-maintaining pump and mixing the thermally hydrolyzed biological sludge with the primary sludge in the pressurized structure; and
wherein neither the thermally hydrolyzed biological sludge nor the sludge mixture is cooled by heat exchangers upstream of the pasteurization unit.

8. The method of claim 1 wherein the method includes first and second modes of operation; and wherein prior to directing the biological sludge to the thermal hydrolysis unit, the method includes directing the biological sludge to one or more dewatering devices and dewatering the biological sludge; and in the first mode of operation the method includes directing the dewatered biological sludge to the thermal hydrolysis unit and in the second mode of operation at least a portion of the dewatered biological sludge is directed to a mixing tank and mixed with the primary sludge prior to the primary sludge reaching the pressurized structure.

9. The method of claim 1 further including cooling the thermal hydrolyzed biological sludge by mixing treated effluent produced by the biological treatment with the thermal hydrolyzed biological sludge.

10. The method of claim 1 further including bypassing the thermal hydrolysis unit with the primary sludge and not subjecting the primary sludge to thermal hydrolysis.

11. The method of claim 1 wherein the pressurized structure extends from the thermal hydrolysis unit to the pasteurization unit and the method includes injecting the primary sludge into the pressurized structure at a point between the thermal hydrolysis unit and the pasteurization unit and mixing the primary sludge with the thermal hydrolyzed biological sludge in the pressurized structure prior to the sludge mixture reaching the pasteurization unit.

12. The method of claim 1 wherein after mixing the thermally hydrolyzed biological sludge with the primary sludge, directing the sludge mixture to the pasteurization unit and pasteurizing the sludge mixture in the pasteurization unit at a temperature of at least 70° C. for a period of at least 20 minutes.

13. The method of claim 1 including preheating the primary sludge prior to the primary sludge being mixed with the thermally hydrolyzed biological sludge.

14. The method of claim 1 wherein pasteurizing the sludge mixture produces a pasteuri

Assignees

• Veolia Water Solutions And Tech Support
• Veolia Water Solutions & Tech

Inventors

• Dimassimo Richard W
• Hojsgaard Soren J

Classifications

• C02F11/185

  by pasteurisation · CPC title

• C02F1/025

  Thermal hydrolysis · CPC title

• C02F11/18

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

• C02F2301/046

  Recirculation with an external loop · CPC title

• C02F2301/043

  Treatment of partial or bypass streams · CPC title