Anaerobic digestion and pyrolysis system

Patent metadata

Field	Value
Publication number	US-11286507-B2
Application number	US-201414903904-A
Country	US
Kind code	B2
Filing date	Jul 11, 2014
Priority date	Jul 11, 2013
Publication date	Mar 29, 2022
Grant date	Mar 29, 2022

Abstract

An anaerobic digester is fed a feedstock, for example sludge from a municipal wastewater treatment plant, and produces a digestate. The digestate is dewatered into a cake. The cake may be dried further, for example in a thermal drier. The cake is treated in a pyrolysis system to produce a synthesis gas and biochar. The gas is sent to the same or another digester to increase its methane production. The char may be used as a soil enhancer.

First claim

We claim:

1. A process comprising steps of,
a) producing a gas including condensable vapors and non-condensable gasses from pyrolysis of a feedstock at a temperature of 400° C. or more; and,
b) adding the gas to an anaerobic digester, wherein the condensable vapors are added in either vapor or liquid form,
wherein the feedstock comprises biomass and plastic.

2. The process of claim 1 wherein the biomass comprises one or more of a raw biomass, wood, municipal yard waste, municipal solids waste, primary sludge from a wastewater treatment plant, waste activated sludge from a wastewater treatment plant, an agricultural waste or residue, and refuse derived fuel.

3. The process of claim 1 wherein the biomass comprises digestate.

4. The process of claim 1 wherein the biomass comprises digestate and one or more of a raw biomass, wood, municipal yard waste, municipal solids waste, primary sludge from a wastewater treatment plant, waste activated sludge from a wastewater treatment plant, an agricultural waste or residue, and refuse derived fuel.

5. The process of claim 3 wherein the digestate is produced by the anaerobic digester or another anaerobic digester receiving a similar feed or both.

6. The process of claim 1 wherein the anaerobic digester is coupled with or part of a municipal wastewater treatment plant, or an agricultural or industrial digester.

7. The process of claim 1 wherein the gas is cooled before it is fed to the digester.

8. The process of claim 1 wherein vapors of condensable organic compounds are removed from the gas and returned as feedstock to step a).

9. The process of claim 1 comprising, before step a), a step of heating the feedstock wherein the heating step comprises contacting the feedstock with a medium at a higher temperature than a heating medium used in step a).

10. The process of claim 1 comprising wherein in step a) the feedstock is pyrolyzed for 15 minutes or more.

11. The process of claim 1 wherein the vapor portion of the gas has a carbon content of 25 wt % or more.

12. The process of claim 1 wherein in step a) the feedstock is pyrolyzed at a temperature of 550 degrees C. or less.

13. The process of claim 1 wherein the vapor portion of the gas has a carbon content of 30 wt % or more.

14. The process of claim 1 , wherein adding the gas to an anaerobic digester comprises adding gas to digestate from the anaerobic digester.

15. The process of claim 14 , wherein the gas is added to digestate in a recirculating digestate loop.

16. The process of claim 15 , further comprising adding a portion of the mixture of gasses from the anaerobic digester to the digestate in the recirculating digestate loop.

Assignees

• Anaergia Inc

Inventors

• Josse Juan Carlos
• Benedek Andrew
• Theodoulou Michael David

Classifications

• Y02W10/40

  Valorisation of by-products of wastewater, sewage or sludge processing · CPC title

• C12M45/20

  Heating; Cooling (heating or cooling apparatus for laboratory uses B01L7/00) · CPC title

• C12P5/023 Primary

  Methane · CPC title

• Y02W10/20

  Sludge processing · CPC title

• Y02E50/10

  Biofuels, e.g. bio-diesel · CPC title