System and process for refining lignocellulosic biomass material

Patent metadata

Field	Value
Publication number	US-12305329-B2
Application number	US-202017434862-A
Country	US
Kind code	B2
Filing date	Feb 12, 2020
Priority date	Mar 1, 2019
Publication date	May 20, 2025
Grant date	May 20, 2025

Abstract

A system ( 1 ) for refining lignocellulosic biomass material (A) comprising a presteaming bin ( 2 ), a dewatering device ( 3 ), a preheater ( 4 ), a defibrator ( 9 ) comprising at least one refining zone ( 14 ) wherein steam is generated during refining of said biomass material so that a pressure peak occurs, a blowpipe ( 19 ), and a first steam flow path (D) arranged to convey steam from said refining zone to said presteaming bin ( 2 ). The system further comprises a second steam flow path (E) arranged to convey steam from said refining zone to said presteaming bin, wherein said first and second steam flow paths are connected to the refining zone on opposite sides of the pressure peakin a biomass material transport direction, and wherein said first and second steam flow paths are separate from said blow pipe. The invention also relates to a process for refining lignocellulosic biomass material.

First claim

The invention claimed is:

1. A system for refining lignocellulosic biomass material, the system comprising:
a presteaming bin for presteaming the biomass material;
a dewatering device for dewatering the biomass material, the dewatering device being downstream of the presteaming bin in a biomass material transport direction;
a preheater for preheating the biomass material, the preheater being downstream of the dewatering device in the biomass material transport direction;
a defibrator comprising at least one refining zone configured to refine the biomass material, wherein steam is generated during the refining of the biomass material such that a pressure peak occurs in the refining zone;
a blow pipe for conveying the biomass material away from the refining zone;
a first steam flow path arranged to convey a first portion of the steam flowing away from the pressure peak against the biomass material transport direction from the refining zone to the presteaming bin; and
a second steam flow path arranged to convey a second portion of the steam flowing away from the pressure peak in the biomass material transport direction from the refining zone to the presteaming bin;
wherein the first and second steam flow paths are connected to the refining zone on opposite sides of the pressure peak in the biomass material transport direction; and
wherein the first and second steam flow paths are separate from the blow pipe.

2. The system according to claim 1 , wherein at least one of the first steam flow path or the second steam flow path comprises at least a portion of the preheater.

3. The system according to claim 1 , wherein the first steam flow path comprises at least a portion of a screw feeder arranged to convey the biomass material to the defibrator.

4. The system according to claim 1 , wherein the dewatering device is a plug screw feeder arranged to convey the biomass material towards the preheater.

5. The system according to claim 1 , wherein:
the refining zone is defined by two opposing refining surfaces accommodated within a grinding house; and
at least one of the refining surfaces is rotatable around an axis of rotation relative the other refining surface.

6. The system according to claim 5 , wherein the blow pipe is connected to a peripheral portion of the grinding house and the first and second steam flow paths are connected to the refining zone inside of the peripheral portion.

7. The system according to claim 1 , further comprising:
a first conduit fluidly coupled between the defibrator and the preheater, wherein the first steam flow path comprises at least a portion of the first conduit; and
a second conduit fluidly coupled between the preheater and the presteaming bin, wherein the first steam flow path comprises at least a portion of the second conduit.

8. The system according to claim 7 , further comprising:
a third conduit fluidly coupled between the defibrator and the presteaming bin, wherein the second steam flow path comprises at least a portion of the third conduit.

9. The system according to claim 8 , wherein the third conduit is directly coupled between the defibrator and the presteaming bin such that the second portion of the steam is conveyed directly from the defibrator to the presteaming bin through the third conduit.

10. A process for refining lignocellulosic biomass material, the process comprising the steps of:
presteaming the biomass material in a presteaming bin;
dewatering the biomass material in a dewatering device, the dewatering device downstream of the presteaming bin in a biomass material transport direction;
preheating the biomass material in a preheater, the preheater downstream of the dewatering device in the biomass material transport direction;
refining the biomass material in a refining zone in a defibrator and generating steam during the refining of the biomass material such that a pressure peak occurs in the refining zone;
conveying the biomass material away from the refining zone via a blow pipe;
conveying a first portion of the steam flowing away from the pressure peak against the biomass material transport direction from the refining zone to the presteaming bin via a first steam flow path; and
conveying a second portion of the steam flowing away from the pressure peak in the biomass material transport direction from the refining zone to the presteaming bin via a second steam flow path;
wherein the first and second steam flow paths are connected to the refining zone on opposite sides of the pressure peak in the biomass material transport direction; and
wherein the first and second steam flow paths are separate from the blow pipe.

11. The process according to claim 10 , wherein at least one of the first steam flow path or the second steam flow path comprises at least a portion of the preheater.

12. The process according to claim 10 , wherein the first steam flow path comprises at least a portion of a screw feeder arranged to convey biomass material to the defibrator.

13. The process according to claim 10 , wherein the refining zone is defined by two opposing refining surfaces accommodated within a grinding house, wherein at least one of the refining surfaces is rotatable around an axis of rotation relative the other refining surface.

14. The process according to claim 13 , wherein the blow pipe is connected to a peripheral portion of the grinding house and the first and second steam flow paths are connected to the refining zone inside of the peripheral portion.

15. The process according to claim 10 , wherein the first steam flow path comprises:
at least a portion of a first conduit fluidly coupled between the defibrator and the preheater; and
at least a portion of a second conduit fluidly coupled between the preheater and the presteaming bin.

16. The process according to claim 15 , wherein the second steam flow path comprises at least a portion of a third conduit fluidly coupled between the defibrator and the presteaming bin.

17. The process according to claim 16 , wherein the third conduit is directly coupled between the defibrator and the presteaming bin such that the second steam flow path extends directly from the defibrator to the presteaming bin through the third conduit.

Assignees

• Valmet Oy

Inventors

• Eriksson Per

Classifications

• D21D1/40

  Washing the fibres · CPC title

• D21D1/30

  Disc mills · CPC title

• D21B1/12

  by wet methods, by the use of steam (beaters D21D1/00) · CPC title

• D21B1/30 Primary

  Defibrating by other means · CPC title

• D21B1/14 Primary

  Disintegrating in mills · CPC title