IP Library Granted Patent US 9,416,374
Granted Patent B2
US 9,416,374 · App. 14/631,144 · Granted Aug 16, 2016

Method for treating lignocellulose-bearing materials

Inventor: F. Michael Lewis (El Segundo, CA)
Assignee: ANAERGIA INC.
C12P7/08C10B47/44C10B53/02C10C5/00C10J3/007C10L3/08C12M21/12C12M29/00C12M43/00C12P5/023C12P7/10C12P7/14C10J2200/158C10J2300/0946C10J2300/1681Y02E50/14Y02E50/16Y02E50/32Y02E50/343
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Quick Facts
Patent No.
US 9,416,374
App. No.
14/631,144
Granted
Aug 16, 2016
Kind
B2
Abstract

A method for the treatment of lignocellulose-containing materials wherein such lignocellulose-containing materials, normally resistant to biotreatment, are first subjected to pyrolysis to produce pyrolysis products including pyrogas and char. Exemplary applications of the method include pyrolytic pre-treatment of wastewater sludges, cellulosic wastes, wood, peat, plant residues, low-grade coal, and the like. The pyrogas is introduced into digester sludge in an anaerobic digester.

Claims (11)

1. A process for treating lignocellulose-bearing materials comprising the steps of,

subjecting one or more first lignocellulose-bearing materials to treatment in an anaerobic digester to produce digester sludge,

subjecting one or more second lignocellulose-bearing materials to pyrolysis to produce pyrolysis products including at least a pyrogas and char, and

introducing the pyrogas into digester sludge in the anaerobic digester.

2. The process of claim 1 wherein the one or more second lignocellulose-bearing materials comprise digester sludge released from the anaerobic digester and undigested lignocellulosic material.

3. The process of claim 1 wherein the one or more second lignocellulose-bearing materials comprise municipal solid waste.

4. The process of claim 1 wherein the one or more second lignocellulose-bearing materials comprise digester sludge released from the anaerobic digester.

5. The process of claim 1 further comprising steps of: separating condensable gasses from the pyrolysis products, condensing the condensable gasses into a liquid, separating the liquid into an aqueous phase and one or more toxic phases, and adding the aqueous phase to the digester sludge in the anaerobic digester.

6. The process of claim 1 wherein the pyrolysis is conducted with a solids residence time of between about 0.1 hours and about 2 hours.

7. The process of claim 1 wherein the pyrogas is injected into a stream of recycled biosolids returning to the anaerobic digester.

8. The process of claim 1 wherein the pyrogas is injected directly into the anaerobic digester.

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 Jul 12, 2016
From: LEWIS, F. MICHAEL
To: ANAERGIA INC.
Reel/Frame 039132/0343 →
Continuity (4)
Continuation 14031758 · Sep 19, 2013
Continuation 13136180 · Jul 26, 2011
Provisional Application 61404005 · Sep 24, 2010
Related Publication 20150167026A1 · Jun 18, 2015