Method for converting biomass to methane
US-8993288-B2 · Mar 31, 2015 · US
US9416374B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9416374-B2 |
| Application number | US-201514631144-A |
| Country | US |
| Kind code | B2 |
| Filing date | Feb 25, 2015 |
| Priority date | Sep 24, 2010 |
| Publication date | Aug 16, 2016 |
| Grant date | Aug 16, 2016 |
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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.
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I claim: 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.
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