Slurry drying plant, a method for drying slurry and use of a slurry drying plant

Patent metadata

Field	Value
Publication number	US-11187458-B2
Application number	US-201816485332-A
Country	US
Kind code	B2
Filing date	Feb 9, 2018
Priority date	Feb 13, 2017
Publication date	Nov 30, 2021
Grant date	Nov 30, 2021

Abstract

Disclosed is a slurry drying plant (1) comprising a slurry inlet (2) for feeding slurry to the slurry drying plant (1) and two or more meshing screw conveyors (3, 4) arranged to at least partly divide the slurry while conveying the slurry in a transport direction from the slurry inlet (2) to a slurry outlet (5). The slurry drying plant (1) further includes slurry heating means (6) comprising means for passing superheated steam substantially at atmospheric pressure past the slurry and the two or more meshing screw conveyors (3, 4), while they are conveying the slurry. Furthermore, a method for drying slurry and use of a slurry drying plant (1) is disclosed.

First claim

The invention claimed is:

1. A slurry drying plant comprising:
a slurry inlet for feeding slurry to said slurry drying plant;
two or more meshing screw conveyors arranged to at least partly divide said slurry while conveying said slurry in a transport direction from said slurry inlet to a slurry outlet; and
a slurry heater for passing superheated steam substantially at atmospheric pressure past said slurry and said two or more meshing screw conveyors while the two or more meshing screw conveyors are conveying said slurry,
wherein said two or more meshing screw conveyors comprise a first screw conveyor and a second screw conveyor, said first screw conveyor meshing with said second screw conveyor.

2. The slurry drying plant according to claim 1 , wherein said first screw conveyor includes a first screw conveyor helical blade running in a first direction around a first screw conveyor rotational axis, said second screw conveyor includes a second screw conveyor helical screw blade running in a second direction around a second screw conveyor rotational axis and wherein said first direction is opposite said second direction.

3. The slurry drying plant according to claim 2 , wherein said first screw conveyor is arranged to rotate in an opposite direction of said second screw conveyor.

4. The slurry drying plant according to claim 1 , wherein said slurry heater comprises a flow duct arranged to let said superheated steam flow past said slurry and said two or more meshing screw conveyors substantially in an opposite direction of said transport direction.

5. The slurry drying plant according to claim 4 , wherein said flow duct comprises a steam inlet for said superheated steam arranged at said slurry outlet and a steam outlet for said superheated steam arranged at said slurry inlet.

6. The slurry drying plant according to claim 1 , wherein said slurry heater comprises a steam heater for heating said superheated steam to an entrance temperature of between 110° C. and 400° C., between 130° C. and 300° C., or between 150° C. and 250° C.

7. The slurry drying plant according to claim 1 , wherein said slurry drying plant further comprises a subsequent thermal processing device in which slurry leaving said slurry outlet is burned or pyrolyzed.

8. The slurry drying plant according to claim 7 , wherein said slurry drying plant further comprises a heat transferrer or for transferring heat generated in or by said subsequent thermal processing device to said superheated steam.

9. The slurry drying plant according to claim 1 , wherein said first screw conveyor rotational axis and said second screw conveyor rotational axis are substantially parallel.

10. The slurry drying plant according to claim 1 , wherein said slurry drying plant further comprises a pressure regulating pump arranged to maintain a steam pressure inside said slurry drying plant substantially at atmospheric pressure.

11. The slurry drying plant according to claim 10 , wherein said pressure regulating pump is arranged to maintain said steam pressure inside said slurry drying plant down to 0.005 Bar or down to 0.001 Bar below an exact atmospheric pressure.

12. A method for drying slurry, said method comprising:
conveying said slurry from a slurry inlet to a slurry outlet by two or more meshing screw conveyors;
divide at least a part of said slurry by said two or more meshing screw conveyors while conveying said slurry from said slurry inlet to said slurry outlet; and
drying said slurry by guiding superheated steam substantially at atmospheric pressure past said slurry and said two or more meshing screw conveyors during said conveying process and dividing at least said part of said slurry so that said superheated steam is in direct contact with at least a part of said slurry and at least parts of said two or more meshing screw conveyors,
wherein said two or more meshing screw conveyors comprise a first screw conveyor and a second screw conveyor, said first screw conveyor meshing with said second screw conveyor.

13. The method according to claim 12 , further comprising:
leading said slurry from said slurry outlet to a subsequent thermal processing device in which said slurry will be burned or pyrolyzed.

14. The method according to claim 12 , further comprising:
transferring heat generated in or by said subsequent thermal processing device to said superheated steam.

15. The method according to claim 12 , wherein the slurry comprises a solid matter content above 2%, above 5%, or above 10%.

Assignees

• Univ Danmarks Tekniske
• Aquagreen License Aps

Inventors

• Ahrenfeldt Jesper
• Henriksen Ulrik Birk
• Thulstrup Claus

Classifications

• F26B21/452

  characterised by the steam generating means · CPC title

• F26B23/02

  using combustion heating ({F26B3/305, F26B13/186, F26B21/001, } F26B23/10 take precedence) · CPC title

• F26B17/20 Primary

  the axis of rotation being horizontal or slightly inclined · CPC title

• F26B2200/18

  Sludges, e.g. sewage, waste, industrial processes, cooling towers · CPC title

• F26B3/06 Primary

  the gas or vapour flowing through the materials or objects to be dried (F26B3/14 takes precedence) · CPC title