IP Library Granted Patent US 11,021,381
Granted Patent B2
US 11,021,381 · App. 16/722,061 · Granted Jun 1, 2021

Two stage anaerobic digestion with intermediate hydrolysis

Inventors: Matthew John Kuzma (Encinitas, CA); Juan Carlos Josse (Aliso Viejo, CA)
Assignee: ANAERGIA INC.
C02F3/286C02F1/025C02F11/04C02F1/20C02F11/125C02F11/18C02F2301/08
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Quick Facts
Patent No.
US 11,021,381
App. No.
16/722,061
Granted
Jun 1, 2021
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 (21)

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

feeding the WWTP or other sludge to an anaerobic digester;

thickening or dewatering digestate from the first anaerobic digester;

hydrolysing a first portion of the thickened or dewatered digestate;

returning a second portion of the thickened or dewatered digestate to the anaerobic digester.

2. The process of claim 1 comprising feeding the hydrolysis product at 15% 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 anaerobic digester while thickening or dewatering the digestate from the 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 feeding the hydrolysis product to a second anaerobic digester and stirring the second anaerobic digester with an electric or hydraulic powered mixer.

8. The process of claim 1 comprising operating the anaerobic digester at 3-8% DS.

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

10. The process of claim 1 wherein the second portion of the thickened or dewater digestate returns to the anaerobic digester at 15% DS or more.

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

an anaerobic digester;

a sludge thickener or dewaterer downstream of the anaerobic digester; and,

a hydrolysis unit downstream of the anaerobic digester,

a recycle loop from between the sludge thickener or dewaterer and the hydrolysis unit to the anaerobic digester.

12. The system of claim 11 wherein the sludge thickener or dewaterer has a solids fraction outlet and a liquid fraction outlet, and the liquid fraction outlet is connected to a WWTP.

13. The system of claim 11 comprising a second anaerobic digester downstream of the hydrolysis unit.

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 051340/0686 →
Continuity (3)
Continuation 15671704 · Aug 8, 2017
Provisional Application 62377946 · Aug 22, 2016
Related Publication 20200123035A1 · Apr 23, 2020