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:
Dec. 19, 2017

Filed:

Oct. 07, 2015
Applicant:

Anaergia Inc., Burlington, CA;

Inventors:

Juan Carlos Josse, Mission Viejo, CA (US);

Andrew Benedek, Rancho Santa Fe, CA (US);

Diana Mourato-Benedek, Rancho Santa Fe, CA (US);

Assignee:

Anaergia Inc., Burlington, CA;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C02F 11/04 (2006.01); C02F 3/28 (2006.01); C02F 9/00 (2006.01); C02F 3/34 (2006.01); C02F 1/28 (2006.01); C02F 1/52 (2006.01); C02F 3/00 (2006.01); C02F 3/12 (2006.01); C02F 3/20 (2006.01); C02F 3/30 (2006.01); C02F 101/16 (2006.01);
U.S. Cl.
CPC ...
C02F 11/04 (2013.01); C02F 3/28 (2013.01); C02F 3/302 (2013.01); C02F 3/34 (2013.01); C02F 9/00 (2013.01); C02F 1/28 (2013.01); C02F 1/52 (2013.01); C02F 3/006 (2013.01); C02F 3/1268 (2013.01); C02F 3/1273 (2013.01); C02F 3/208 (2013.01); C02F 3/286 (2013.01); C02F 3/2826 (2013.01); C02F 3/2833 (2013.01); C02F 3/2846 (2013.01); C02F 3/2873 (2013.01); C02F 3/307 (2013.01); C02F 3/308 (2013.01); C02F 2101/16 (2013.01); C02F 2209/08 (2013.01); C02F 2209/10 (2013.01); C02F 2209/225 (2013.01); C02F 2303/02 (2013.01); C02F 2303/20 (2013.01); C02F 2303/24 (2013.01); Y02E 50/343 (2013.01); Y02W 10/12 (2015.05); Y02W 10/15 (2015.05); Y02W 10/23 (2015.05);
Abstract

Low strength wastewater such as municipal sewage is treated using an anaerobic digester. In some examples, a wastewater stream is separated into a solids rich portion and a solids lean portion. The solids lean portion is treated, for example to remove nitrogen. The solids rich portion is treated in an anaerobic digester, preferably with influent or recuperative thickening. In another example, the wastewater stream is fed to an anaerobic digester and solid-liquid separation stages downstream of the digester return active bacteria and undigested organics to the digester. Both cases may use a process train comprising treatment in an anoxic tank followed by a nitritation tank with a portion of the effluent from the nitritation tank recirculated to the anoxic tank to provide nitritation and denitritation.


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