IP Library Granted Patent US 10,550,023
Granted Patent B2
US 10,550,023 · App. 15/671,704 · Granted Feb 4, 2020

Two stage anaerobic digestion with intermediate hydrolysis

Inventors: Matthew John Kuzma (Encinitas, CA); Juan Carlos Josse (Mission Viejo, CA)
Assignee: Anaergia Inc.
C02F3/286C02F1/025C02F11/04C02F1/20C02F11/125C02F11/18C02F2301/08
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Quick Facts
Patent No.
US 10,550,023
App. No.
15/671,704
Granted
Feb 4, 2020
Kind
B2
Abstract

In a system and process, sludge is treated by two stages of anaerobic digestion in series separated by intermediate thickening and hydrolysis. The hydrolysis product is transferred to the second digester essentially without dilution.

Claims (18)

1. A process for treating wastewater treatment plant (WWTP) or other sludge comprising the steps of,

feeding the WWTP or other sludge to a first anaerobic digester;

thickening the WWTP or other sludge to 8% DS or more before feeding to the first anaerobic digester and/or recuperative thickening the digestate from the first anaerobic digester;

thickening or dewatering the digestate from the first anaerobic digester;

hydrolysing the thickened or dewatered digestate;

feeding the hydrolysis product at 15% DS or more to a second anaerobic digester.

2. The process of claim 1 comprising feeding the hydrolysis product at 16% DS or more to a second anaerobic digester.

3. The process of claim 1 comprising feeding the hydrolysis product at 18% DS or more to a second anaerobic digester.

4. The process of claim 1 comprising feeding the hydrolysis product at 20% DS or more to a second anaerobic digester.

5. The process of claim 1 comprising producing a liquid fraction of the digestate from the first anaerobic digester while thickening or dewatering the digestate from the first anaerobic digester and removing ammonia from the liquid fraction to produce an ammonia depleted liquid fraction.

6. The process of claim 5 wherein the sludge is from a WWTP and the ammonia depleted liquid fraction is returned to the WWTP.

7. The process of claim 1 comprising stirring the second anaerobic digester with an electric or hydraulic powered mixer.

8. The process of claim 1 wherein the step of thickening the WWTP or other sludge to 8% DS or more before feeding to the first anaerobic digester and/or recuperative thickening the digestate from the first anaerobic digester consists of recuperative thickening the digestate from the first anaerobic digester.

9. A system for treating WWTP or other sludges comprising,

two or more anaerobic digesters with a) a sludge thickener or dewaterer and b) a hydrolysis unit, in series between two of the two or more anaerobic digesters; and

a sludge thickener upstream of the two or more anaerobic digesters and/or a recuperative thickening loop in series and between a) the sludge thickener or dewaterer and b) the hydrolysis unit.

10. The system of claim 9 wherein the sludge thickener or dewaterer has a solids fraction outlet and a liquid fraction outlet, the solids fraction outlet is connected to a downstream one of the two or more anaerobic digesters and the liquid fraction outlet is connected to a WWTP.

11. The system of claim 9 wherein a downstream one of the two or more anaerobic digesters has an electrically or hydraulically driven mixer.

Assignments (2)
SECURITY INTEREST Recorded May 7, 2026
From: ANAERGIA INC.
To: NATIONAL BANK OF CANADA
Reel/Frame 074589/0942 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Dec 20, 2019
From: KUZMA, MATTHEW JOHN; JOSSE, JUAN CARLOS
To: ANAERGIA INC.
Reel/Frame 051340/0233 →
Continuity (2)
Provisional Application 62377946 · Aug 22, 2016
Related Publication 20180050941A1 · Feb 22, 2018