DEVICE AND METHOD FOR THE DRYING AND TORREFACTION OF AT LEAST ONE CARBON-CONTAINING MATERIAL FLOW IN A MULTIPLE HEARTH FURNACE

• US 20120137538A1
• Filed: 07/15/2011
• Published: 06/07/2012
• Est. Priority Date: 07/15/2010
• Status: Active Grant

• Current Assignee: ThyssenKrupp Industrial Solutions AG (Thyssenkrupp AG)
• Original Assignee: ThyssenKrupp Industrial Solutions AG (Thyssenkrupp AG)
• Inventors: Beyer, Christoph, Erpelding, Richard, Lampe, Karl, Denker, Jürgen
• Granted Patent: US 9,102,876 B2
• Time in Patent Office: Days
• US Class Current: 34/487
• CPC Class Codes: C10B 49/02 with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
• CPC Class Codes: C10B 53/02 of cellulose-containing material production of pyroligneous acid C10C5/00
• CPC Class Codes: C10B 7/02 with rotary scraping devices
• CPC Class Codes: C10L 5/40 essentially based on materials of non-mineral origin
• CPC Class Codes: C10L 9/083 Torrefaction
• CPC Class Codes: F26B 17/003 with fixed floors provided with scrapers F26B17/006 and F26B17/007 take precedence
• CPC Class Codes: F26B 21/04 partly outside the drying enclosure F26B21/006 takes precedence
• CPC Class Codes: F26B 21/14 using gases or vapours other than air or steam , e.g. inert gases
• CPC Class Codes: F26B 2200/02 Biomass, e.g. waste vegetative matter, straw
• CPC Class Codes: F26B 23/022 incinerating volatiles in the dryer exhaust gases, the produced hot gases being wholly, partly or not recycled into the drying enclosure
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel
• CPC Class Codes: Y02E 50/30 Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

The device according to the invention for drying and torrefaction of at least one carbon-containing material flow in a multiple-hearth furnace substantially comprises

a drying zone, which comprises a feed device for feeding a carbon-containing material flow, a discharge point for discharging a drying gas flow containing water vapour and an infeed point for recycling at least a part of the drying gas flow,
a torrefaction zone for degassing the material flow dried in the drying zone, which comprises a discharge point for discharging a torrefied material flow, at least one infeed point for an exhaust gas and a discharge point for a torrefaction gas flow,
a heat exchanger for heating the drying gas flow, the discharge point of the drying zone being connected via the heat exchanger to the infeed point of the drying zone,
a combustion assembly, wherein the discharge point of the torrefaction zone is connected via the combustion assembly and the heat exchanger to the infeed point of the torrefaction zone,
wherein a torrefaction gas flow discharged via the discharge point of the torrefaction zone is combusted in the combustion assembly and the resulting exhaust gas is used in the heat exchanger to heat the drying gas flow and is fed to the torrefaction zone,
wherein the drying zone and the torrefaction zone comprise two separate gas circulations.

Claims

1. A device for drying and torrefaction of at least one carbon-containing material flow in a multiple-hearth furnace, comprising

a. a drying zone, which comprises a feed device for feeding a carbon-containing material flow, a discharge point for discharging a drying gas flow containing water vapour and an infeed point for recycling at least a part of the drying gas flow,

b. a torrefaction zone for degassing the material flow dried in the drying zone, which comprises a discharge point for discharging a torrefied material flow, at least one infeed point for an exhaust gas and a discharge point for a torrefaction gas flow,

c. a heat exchanger for heating the drying gas flow, the discharge point of the drying zone being connected via the heat exchanger to the infeed point of the drying zone,

d. a combustion assembly, wherein the discharge point of the torrefaction zone is connected via the combustion assembly and the heat exchanger to the infeed point of the torrefaction zone,

e. wherein a torrefaction gas flow discharged via the discharge point of the torrefaction zone is combusted in the combustion assembly and the resulting exhaust gas is used in the heat exchanger to heat the drying gas flow and is fed to the torrefaction zone,

f. wherein the drying zone and the torrefaction zone comprise two separate gas circulations.

2. A device according to claim 1, characterised in that the heat exchanger comprises a first inlet and a first outlet connected thereto, as well as a second inlet and a second outlet connected thereto, the first inlet being connected to discharge point of the drying zone and the first outlet being connected to the infeed point of the drying zone, and furthermore the second inlet is connected via the combustion assembly to the discharge point of the torrefaction zone and the second outlet is connected to the infeed point, of the torrefaction zone.

3. A device according to claim 1, characterised in that the drying zone and/or the torrefaction zone each comprise a plurality of hearths arranged one above the other.

4. A device according to claim 1, characterised in that a mechanical transfer device for transferring the dried, carbon-containing material flow is provided between the drying zone and the torrefaction zone.

5. A device according to claim 4, characterised in that the transfer device between the drying and torrefaction zone is of gas-tight construction in order to prevent mixing of the two gas circulations.

6. A device according to claim 1, characterised in that the multiple-hearth furnace comprises transport devices for transporting the material flow, which are driven via a drive shaft, which is divided between the drying zone and torrefaction zone and is equipped with a separate drive for each zone in order to be able to change the residence times of the carbon-containing material flow in the two zones independently of one another by way of the respective speed of rotation.

7. A device according to claim 1, characterised in that a condenser is inserted between the discharge point of the torrefaction zone and the combustion assembly.

8. A device according to claim 1, characterised in that the combustion assembly is formed by a burner or an internal combustion engine.

9. A method for drying and torrefaction of at least one carbon-containing material flow in a multiple-hearth furnace, wherein

a. the biomass is dried in a drying zone by means of a drying gas flow and is subsequently torrefied in a torrefaction zone,

b. part of the drying gas flow containing water vapour is discharged from the drying zone and heated in a heat exchanger and then at least partially recycled to the drying zone,

wherein

c. part of a torrefaction gas flow evolving in the torrefaction zone is discharged from the torrefaction zone and fed to a combustion assembly for combustion, wherein the resulting exhaust gas is used to heat the drying gas flow in the heat exchanger and is introduced into the torrefaction zone, and

d. the drying zone and the torrefaction zone are operated with two separate gas circulations.

10. A method according to claim 9, characterised in that the drying zone is operated cocurrently.

11. A method according to claim 9, characterised in that the torrefaction zone is operated countercurrently.

12. A method according to claim 9, characterised in that the temperature of the carbon-containing material flow during transfer into the torrefaction zone is less than 150°

C.

13. A method according to claim 9, characterised in that the drying gas flow in the gas circulation is filtered.

14. A method according to claim 9, characterised in that the water vapour-containing drying gas flow is superheated in the heat exchanger.

15. A method according to claim 14, characterised in that the amount of steam recycled in the drier circulation is so large that an inert atmosphere having an oxygen content of <

10%, preferably <

8% is set.

16. A method according to claim 9, characterised in that the amount of exhaust gas introduced into the torrefaction zone so large that an inert atmosphere having an oxygen content of <

10% is set in the torrefaction zone.

17. A method according to claim 9, characterised in that the temperature of the exhaust gas introduced into the torrefaction zone is more than 300°

C. and the temperature of the recycled drying gas flow is set within the range from 150°

C. to 300°

C.

18. A method according to claim 9, characterised in that exhaust gas is enriched with hot steam before it enters the torrefaction zone.

19. A method according to claim 9, characterised in that before being fed into the combustion assembly, the torrefaction gas flow discharged from the torrefaction zone is introduced into a condenser, in which the condensable constituents are at least partially precipitated and the non-condensable constituents are combusted in the combustion assembly.

20. A method according to claim 9, characterised in that the torrefaction gas flow discharged from the torrefaction zone is combusted in the combustion assembly and is partially converted into mechanical energy.

21. A method according to claim 9, characterised in that in the drying zone and/or torrefaction zone the temperature and/or the gas flow and/or the gas amount and/or the pressure are measured and used for controlling the residence time of the material in the two zones.

22. A method according to claim 9, characterised in that the residence time in the drying zone and torrefaction zone is adjusted by changing the number of hearths, by reducing hearth areas, by changing the design and the number of transport devices or by varying the speed of rotation of transport devices.