The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Sep. 13, 2022

Filed:

Dec. 18, 2018
Applicant:

Veolia Water Solutions & Technologies Support, Saint-Maurice, FR;

Inventors:

Hong W. Zhao, Raleigh, NC (US);

Sudhakar Viswanathan, Cary, NC (US);

Luther G. Wood, Cary, NC (US);

Brad Mrdjenovich, Fuquay Varina, NC (US);

Richard W. DiMassimo, Raleigh, NC (US);

James McQuarrie, Denver, CO (US);

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C02F 11/04 (2006.01); C05F 17/60 (2020.01); C05F 17/40 (2020.01); C02F 9/00 (2006.01); C02F 3/12 (2006.01); C02F 11/12 (2019.01); C02F 11/13 (2019.01); C02F 11/18 (2006.01); C05F 7/00 (2006.01); C02F 1/52 (2006.01); C02F 3/00 (2006.01); C02F 101/10 (2006.01); C02F 101/16 (2006.01);
U.S. Cl.
CPC ...
C02F 11/04 (2013.01); C02F 9/00 (2013.01); C05F 7/005 (2013.01); C05F 17/40 (2020.01); C05F 17/60 (2020.01); C02F 1/5245 (2013.01); C02F 3/006 (2013.01); C02F 3/121 (2013.01); C02F 3/1215 (2013.01); C02F 11/12 (2013.01); C02F 11/13 (2019.01); C02F 11/18 (2013.01); C02F 2101/105 (2013.01); C02F 2101/16 (2013.01); C02F 2209/02 (2013.01); C02F 2209/06 (2013.01); C02F 2209/14 (2013.01); C02F 2209/18 (2013.01); C02F 2301/08 (2013.01);
Abstract

The present invention relates to a method of treating sludge containing phosphorus, ammonia and magnesium and enhancing the dewaterability of the sludge. The sludge is directed into a biological fermenter operated under anaerobic conditions. By controlling the temperature of the sludge in the fermenter or the hydraulic retention time of the sludge in the fermenter, phosphorus, ammonia and magnesium is released from the solids in the sludge into a liquid forming a part of the sludge. Sludge from the fermenter is subjected to a solids-liquid separation process that produces a concentrated sludge and a liquid. The concentrated sludge or separated solids is directed to a thermal hydrolysis reactor that thermally hydrolyzes the concentrated sludge. After thermally hydrolyzing the concentrated sludge, the concentrated sludge is directed to an anaerobic digester that anaerobically digests the concentrated sludge.


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