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. 04, 2018

Filed:

Jul. 13, 2016
Applicant:

Anaergia Inc., Burlington, CA;

Inventor:

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

Assignee:

Anaergia Inc., Burlington, CA;

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C02F 11/04 (2006.01); B01D 61/14 (2006.01); B01D 61/18 (2006.01); C02F 3/28 (2006.01); C12P 5/02 (2006.01); C02F 11/12 (2006.01); C12M 1/107 (2006.01); C12M 1/26 (2006.01); C02F 103/20 (2006.01);
U.S. Cl.
CPC ...
C02F 11/04 (2013.01); B01D 61/145 (2013.01); B01D 61/147 (2013.01); B01D 61/18 (2013.01); C02F 3/2853 (2013.01); C02F 11/121 (2013.01); C12M 21/04 (2013.01); C12M 33/00 (2013.01); C12P 5/023 (2013.01); B01D 2311/04 (2013.01); B01D 2311/25 (2013.01); B01D 2311/2642 (2013.01); B01D 2311/2649 (2013.01); B01D 2315/06 (2013.01); C02F 2103/20 (2013.01); C02F 2203/004 (2013.01); Y02E 50/343 (2013.01);
Abstract

A process and apparatus for the anaerobic digestion of organic wastes, preferably to also produce a useful biogas, is described. The waste may have a total solids (TS) concentration of 6% or less while a digester is operated at a higher solids concentration, for example with a feed TS concentration of 8-12%. One or more separation stages downstream of the digester separate active bacteria and undigested organics from the digestate, and return separated matter to the digester. Optionally, a feed thickening apparatus and step may be provided upstream of the digester. The upstream thickener and recycle from the downstream separation stages are operated such that the TS of the combined inputs to the digester is within a desired range.


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