IP Library Granted Patent US 9,822,020
Granted Patent B2
US 9,822,020 · App. 14/652,615 · Granted Nov 21, 2017

Nutrient recovery process

Inventors: Ashwani Kumar (Mississauga, CA); Juan Carlos Josse (Mission Viejo, CA); Michael David Theodoulou (Milton, CA); Sasha Michael Rollings-Scattergood (Fergus, CA)
Assignee: Anaergia Inc.
C02F1/20C01C1/10C01C1/242C02F11/04C05B17/00C05F17/0018C05F17/0027C05F17/0045C05F17/0054C02F11/12C02F11/121C02F2209/14C02F2303/02Y02P20/145Y02W10/23Y02W30/43Y02W30/47
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Quick Facts
Patent No.
US 9,822,020
App. No.
14/652,615
Granted
Nov 21, 2017
Kind
B2
Abstract

An apparatus for recovering nutrients or water from digestate comprises one or more solid-liquid separation units, an ammonia stripping device, and a gas scrubbing unit. In a process, digestate is separated into a solids portion and a liquid portion. Ammonia is stripped from the liquid portion and converted into an ammonium salt solution which may be sold or used as, or blended with, a fertilizer product. Optionally, at least part of the remaining liquid portion may be concentrated to produce brine. The brine is mixed with the solids portion. The mixture may be dried and used as, or blended with, a fertilizer product. Optionally, a least part of the remaining liquid portion may be re-used as dilution water in a digester. A solids portion of the digestate, and one or both of an ammonium salt solution and a brine, may be used as fertilizer without thermal drying.

Claims (12)

1. A process comprising steps of,

a) separating a solids portion and liquid portion from an anaerobic digester digestate;

b) stripping ammonia from the liquid portion to produce an ammonia stripped liquid; and,

returning 80% or more of the ammonia stripped liquid to the anaerobic digester.

2. The process of claim 1 further comprising a step of passing a mixed gas flow resulting from step b) through a scrubber to produce an ammonium salt solution.

3. The process of claim 2 wherein the ammonium salt solution is added to the solids portion.

4. The process of claim 3 wherein the solids portion is not thermally dried after adding the ammonium salt solution.

5. The process of claim 3 wherein the solids portion is not thermally dried.

6. The process of claim 2 wherein the ammonium salt solution is concentrated by distillation.

7. The process of claim 1 wherein step a) comprises two solid-liquid separation steps.

8. The process of claim 7 wherein a first of the solid-liquid separation steps comprises removing fibers from the digestate.

9. The process of claim 1 wherein step b) comprises heating the liquid to at least 50 degrees C., flowing the ammonia through a series of sequential stages, and blowing bubbles of air into the liquid in the stages.

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 Oct 20, 2017
From: KUMAR, ASHWANI; JOSSE, JUAN CARLOS; THEODOULOU, MICHAEL DAVID; ROLLINGS-SCATTERGOOD, SASHA MICHAEL
To: ANAERGIA INC.
Reel/Frame 043915/0579 →
Priority Claims (1)
WO PCT/CA2012/050907 · Dec 18, 2012 · international
Continuity (3)
Continuation In Part 13832737 · Mar 15, 2013
Provisional Application 61810088 · Apr 9, 2013
Related Publication 20150329399A1 · Nov 19, 2015