Solid waste treatment process

Patent metadata

Field	Value
Publication number	US-11453010-B2
Application number	US-201816157458-A
Country	US
Kind code	B2
Filing date	Oct 11, 2018
Priority date	Oct 13, 2017
Publication date	Sep 27, 2022
Grant date	Sep 27, 2022

Abstract

In an apparatus and process described, an organic fraction of solid waste is separated from light contaminants such as plastics and heavy contaminants such as grit. The organic fraction is subsequently processed by anaerobic digestion, which converts volatile solids to gas. In a first stage of the process, the waste is processed through a separator such as a vertical mill, which removes light fraction contamination, reduces organics particle size and dilutes the waste to thereby produce a slurry. In a second stage of the process, the slurry passes through a grit removal system, which removes heavy and settleable material, for example by way of a hydrocyclone. The light and heavy fraction contaminants are not carried through to the digestion process. The particle size of the organics is also reduced to facilitate digestion and the slurry has a dry solids concentration suitable for anaerobic digestion.

First claim

We claim:

1. A system for processing solid waste comprising,
a light fraction separator configured to separate the solid waste into a light fraction and a slurry;
a grit removal system to produce a de-gritted slurry, the grit removal system comprising one or more grit staging tanks and a hydrocyclone, the one or more grit staging tanks comprising a first portion and a second portion, wherein:
the first portion is in fluid communication with the light fraction separator to accept the slurry and configured to serve as a staging tank before the slurry is sent to the hydrocyclone,
the hydrocyclone is in fluid communication with the first portion and configured to separate the grit from the slurry, and,
the second portion is in fluid communication with the hydrocyclone and configured to accept an overflow from the hydrocyclone,

a recycle flow path connecting the second portion to the first portion; and,
an anaerobic digester configured to receive the de-gritted slurry from the grit removal system.

2. The system of claim 1 wherein the light fraction separator has an inlet for dilution liquid.

3. The system of claim 1 wherein the light fraction separator comprises a vertically oriented rotor inside of a cylindrical wall.

4. The system of claim 3 wherein the rotor comprises one or more macerating or comminuting blades.

5. The system of claim 4 wherein the one or more blades are angled relative to a shaft of the rotor so as to lift solids within the cylindrical wall, and wherein the light fraction is collected from the inside of an upper end of the cylindrical wall.

6. The system of claim 3 wherein the cylindrical wall has a plurality of openings, and wherein the slurry is collected from outside of the cylindrical wall.

7. The system of claim 1 wherein the anaerobic digester comprises a wet digester.

8. The system of claim 1 wherein the grit removal system further comprises a grit washing system.

9. The system of claim 1 wherein the first portion comprises a grit tank and the second portion comprises a clean tank.

10. A process for treating solid waste comprising,
separating the solid waste into a light fraction and a slurry;
de-gritting the slurry by at least treating the slurry in one or more grit staging tanks and a hydrocylone, wherein the de-gritting comprises,
staging the slurry in a first portion of the one or more grit staging tanks before flowing the slurry to the hydrocyclone;
separating grit from the slurry in the hydrocyclone; and,
flowing an overflow of the hydrocyclone to a second portion of the one or more grit staging tanks that is in fluid communication with the first portion;

recycling a portion of the slurry from the second portion of the one or more grit staging tanks back to the first portion of the one or more grit staging tanks; and,
anaerobically digesting the de-gritted slurry.

11. The process of claim 10 wherein the step of separating the solid waste further comprises macerating and/or comminuting the solid waste.

12. The process of claim 11 wherein the step of separating the solid waste comprises adding water to the solid waste.

13. The process of claim 10 wherein the slurry is produced through openings in a wall while the light fraction is retained by the wall.

14. The process of claim 13 wherein the solid waste is diluted and comminuted upstream of the wall.

15. The process of claim 14 wherein the solid waste is treated by a rotor inside of vertically oriented cylindrical wall.

16. The process of claim 10 wherein the slurry has a dried solids content of 12% or less.

17. The process of claim 10 wherein the slurry is treated in a wet anaerobic digester.

18. The process of claim 10 wherein the slurry is treated by hydrolysis prior to anaerobic digestion.

19. The process of claim 18 wherein the slurry is treated by enzymatic hydrolysis.

20. The process of claim 10 wherein the first portion comprises a grit tank and the second portion comprises a clean tank.

Assignees

• Bl Technologies Inc

Inventors

• Theodoulou Michael
• Hong Youngseck
• Braithwaite Nick
• De Backer Marion

Classifications

• B03B9/06 Primary

  specially adapted for refuse · CPC title

• B02C23/20 Primary

  after crushing or disintegrating · CPC title

• Y02W30/62

  Plastics recycling; Rubber recycling · CPC title

• B02C18/0092

  for waste water or for garbage · CPC title

• B01D21/267

  by using a cyclone · CPC title