Method for removing liquid from a slurry

Patent metadata

Field	Value
Publication number	US-11179909-B2
Application number	US-202016829399-A
Country	US
Kind code	B2
Filing date	Mar 25, 2020
Priority date	Jun 13, 2012
Publication date	Nov 23, 2021
Grant date	Nov 23, 2021

Abstract

A method for removing liquid from a slurry includes: (i) feeding the slurry into the inlet of a press; (ii) removing liquid from the slurry as the slurry advances through a deliquifying section of the press, thereby producing a pressate stream; (iii) forming a plug of material as the slurry is advanced through a plug formation section of the press; (iv) advancing the plug of material to a discharge section of the press; and (v) removing additional liquid from the plug of material by operating the press so that the pressure in the discharge section of the press is greater than the pressure of the pressate stream by at least 2 psi. The present invention also relates to a method for controlling discharge consistency from a press, without provision of discharge restrictors, by varying the pressure differential between a discharge section of the press and a pressate stream.

First claim

The invention claimed is:

1. A method of removing liquid from a lignocellulosic feedstock slurry using a press, the press comprising:
an outer shell with an inlet end and an outlet end;
at least one inner shell disposed within the outer shell; and
a conveyance member mounted within the press such that the conveyance member is rotatable within the at least one inner shell around an axis, the conveyance member having a screw section configured to convey slurry from the inlet end towards the outlet end and into a pressurized discharge chamber,
wherein the at least one inner shell comprises a concentric screen having a plurality of openings and a concentric shell adjoining the concentric screen, and wherein each of the concentric screen and the concentric shell surrounds a length of the conveyance member and is coaxial with the conveyance member, the method comprising:

(a) feeding a pressurized slurry into an inlet of the press disposed at the inlet end, said slurry comprising lignocellulosic feedstock;
(b) conveying the slurry fed into the inlet through a space between the conveyance member and the concentric screen, thereby passing at least a portion of liquid in the slurry through the openings while retaining at least some undissolved solids in the slurry;
(c) removing the liquid passed through the openings from a pressate chamber disposed between the concentric screen and the outer shell;
(d) using the conveyance member, pressing the retained undissolved solids into a decreasing space between the conveyance member and the concentric screen, thereby compressing the retained undissolved solids;
(e) advancing the compressed undissolved solids to an annular space between the concentric shell and the conveyance member, thereby compacting the retained undissolved solids and forming an annular plug of material;
(f) advancing the annular plug of material toward the pressurized discharge chamber;
(g) introducing steam or a compressed gas into the pressurized discharge chamber via at least one inlet in the discharge chamber such that a pressure in the pressurized discharge chamber is higher than a pressure in the pressate chamber by at least 2 psi, thereby removing additional liquid from the annular plug of material;
(h) discharging the annular plug material having reduced liquid content, or segments thereof, from the press via an outlet of the press disposed at the outlet end; and
(i) controlling a consistency of the annular plug of material having reduced liquid content, or segments thereof, discharged in step (h), wherein the controlling step (i) comprises adjusting a pressure in the pressate chamber or adjusting a pressure in the pressurized discharge chamber, thereby varying a pressure differential between the pressate chamber and the pressurized discharge chamber, and
wherein the controlling step (i) is conducted without using a variable discharge restrictor.

2. The method according to claim 1 , wherein (i) comprises adjusting a pressure in the pressate chamber using a valve.

3. The method according to claim 2 , wherein (g) comprises introducing steam into the pressurized discharge chamber such that a pressure in the pressurized discharge chamber is higher than a pressure in the pressate chamber by at least 5 psi.

4. The method according to claim 3 , wherein the pressure differential between the pressate chamber and the pressurized discharge chamber is between 10 and 70 psi.

5. The method according to claim 4 , wherein the conveyance member comprises a restricting cone configured to partially obstruct advancement of the annular plug of material.

6. The method according to claim 5 , wherein the conveyance member comprises a plug breaker.

7. The method according to claim 6 , wherein the concentric shell comprises anti-rotation elements configured to reduce or eliminate rotation of the annular plug of material with rotation of the conveyance member.

8. The method according to claim 7 , wherein a consistency the annular plug of material having reduced liquid content, or segments thereof, is between 20 wt % and 35 wt % undissolved solids.

9. The method according to claim 8 , wherein a pressure of the pressurized slurry is between 100 psi and 500 psi.

10. The method according to claim 1 , wherein (g) comprises introducing steam into the pressurized discharge chamber such that a pressure in the pressurized discharge chamber is higher than a pressure in the pressate chamber by at least 5 psi.

11. The method according to claim 1 , wherein the pressure differential between the pressate chamber and the pressurized discharge chamber is between 10 and 70 psi.

12. The method according to claim 1 , wherein the conveyance member comprises a restricting cone configured to partially obstruct advancement of the annular plug of material.

13. The method according to claim 1 , wherein the conveyance member comprises a plug breaker.

14. The method according to claim 1 , wherein the concentric shell comprises anti-rotation elements configured to reduce or eliminate rotation of the annular plug of material with rotation of the conveyance member.

15. The method according to claim 1 , wherein a consistency the annular plug of material having reduced liquid content, or segments thereof, is between 20 wt % and 35 wt % undissolved solids.

16. The method according to claim 15 , wherein the conveyance member has an increasing cross-sectional area from the inlet end towards the outlet end.

17. The method according to claim 1 , wherein a pressure of the pressurized slurry is between 100 psi and 500 psi.

18. The method according to claim 1 , wherein the conveyance member has an increasing cross-sectional area from the inlet end towards the outlet end.

Assignees

• Voith Patent Gmbh
• Iogen Energy Corp

Inventors

• Miller William
• Richardson Trevor
• Rowland Stephen A

Classifications

• Y02E50/10

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

• B30B9/18

  with means for adjusting the outlet for the solid · CPC title

• B30B9/14

  operating with only one screw or worm · CPC title

• C02F11/125

  using screw filters · CPC title

• B30B9/125 Primary

  Control arrangements · CPC title