Apparatus and method for refractory organics conversion into biogas

Patent metadata

Field	Value
Publication number	US-11279908-B2
Application number	US-201816630808-A
Country	US
Kind code	B2
Filing date	Jul 30, 2018
Priority date	Aug 1, 2017
Publication date	Mar 22, 2022
Grant date	Mar 22, 2022

Abstract

An apparatus for refractory organics conversion into biogas includes an anaerobic digester configured to be fed with organic material comprising refractory organics and to generate biogas and a digestate comprising at least a part of the refractory organics, wherein the apparatus comprises a device for a controlled partial oxidation of the refractory organics comprising an inlet configured to be fed with refractory organics and means configured to control the residence time of the refractory organics within the device for a controlled partial oxidation, so as to partially degrade refractory organics. A method for refractory organics conversion into biogas carried out using such an apparatus is also provided.

First claim

The invention claimed is:

1. An apparatus for refractory organics conversion into biogas comprising:
an anaerobic digester configured:
to be fed with organic material comprising refractory organics, and to generate biogas and a digestate comprising at least a part of the refractory organics;

the apparatus further comprising a device for a controlled partial oxidation of the refractory organics, the device for a controlled partial oxidation being a Fenton, the device comprising:
an inlet configured to be fed with refractory organics, and
means configured to control a residence time of the refractory organics within the device for a controlled partial oxidation, so as to partially degrade refractory organics.

2. The apparatus according to claim 1 , wherein the anaerobic digester comprises a recirculation loop configured to recirculate the at least a part of the refractory organics degraded by the device for a controlled partial oxidation back into the anaerobic digester, and wherein the device for a controlled partial oxidation is located on the recirculation loop.

3. The apparatus according to claim 1 , wherein the apparatus comprises a recirculation loop configured to recirculate the refractory organics degraded by the device for a controlled partial oxidation back into the organic material, and wherein the device for a controlled partial oxidation is located on the recirculation loop.

4. The apparatus according to claim 1 , further comprising a dewatering unit configured to dewater the digestate from the anaerobic digester, so as to lead to a solid cake and a liquid centrate.

5. The apparatus according to claim 4 , arranged in such a way that at least a part of the liquid centrate is fed to the device for a controlled partial oxidation connected to an inlet of the anaerobic digester.

6. The apparatus according to claim 1 , further comprising a dewatering unit configured to dewater the organic material, so as to lead to a solid cake and a liquid centrate, the liquid centrate being intended to be fed to the anaerobic digester.

7. The apparatus according to claim 1 , further comprising a unit for H 2 O 2 removal intended to be located downstream of the device for a controlled partial oxidation.

8. The apparatus according to claim 1 , the degradation of the refractory organics leading to a formation of soluble organic molecules, wherein the apparatus further comprises a control loop to control input parameters of the device for a controlled partial oxidation as a function of a quantity of soluble organic molecules downstream of the device for a controlled partial oxidation.

9. The apparatus according to claim 8 , wherein said soluble organic molecules are chosen among the group comprising volatile fatty acids, sugars, amino acids, fatty acids, monomers, oligomers.

10. A method for refractory COD conversion into biogas within an apparatus for refractory organics conversion into biogas comprising an anaerobic digester configured to be fed with organic material comprising refractory COD and to generate biogas and a digestate comprising at least a part of the refractory organics,
the method comprising:
a step of providing refractory organics to a device for a controlled partial oxidation of the refractory organics, the device for a controlled partial oxidation being a Fenton;
a step of controlling a residence time of the refractory organics within the device for a controlled partial oxidation, so as to partially degrade the refractory organics.

11. The method according to claim 10 , further comprising a step of recirculating the refractory organics degraded by the device for a controlled partial oxidation in a recirculation loop back into the anaerobic digester and/or the organic material.

12. The method according to claim 11 , further comprising a step of feeding the digestate from the anaerobic digester into a dewatering unit configured to dewater the digestate from the anaerobic digester, leading to a solid cake and a liquid centrate.

13. The method according to claim 12 , further comprising a step of feeding at least a part of the liquid centrate to the device for a controlled partial oxidation connected to an inlet of the anaerobic digester.

14. The method according to claim 10 , further comprising a step of feeding the organic material into a dewatering unit, so as to lead to a solid cake and a liquid centrate, the liquid centrate being fed to the anaerobic digester.

15. The method according to claim 10 , further comprising a step of feeding an outlet of the device for a controlled partial oxidation to a unit for H 2 O 2 removal.

16. The method according to claim 10 , further comprising a step of controlling input parameters of the device for a controlled partial oxidation as a function of a quantity of soluble organic molecules formed by the degradation of the refractory organics downstream of the device for a controlled partial oxidation.

Assignees

• Suez Groupe

Inventors

• Camacho Patricia
• Haddad Mathieu

Classifications

• C02F2305/026

  Fenton's reagent · CPC title

• C02F11/04

  Anaerobic treatment; Production of methane by such processes · CPC title

• C02F1/722

  Oxidation by peroxides · CPC title

• C02F3/28

  Anaerobic digestion processes · CPC title

• C02F2103/06

  Contaminated groundwater or leachate · CPC title