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Key Issues in Torrefaction
Process Plant Design and
Operation
B. Greenwood (Andritz Inc)
B. Stromberg (Andritz Inc)
A. Eyer (Andritz Inc)
D. Thamer (Andritz AG)
K. Trattner (Andritz AG)
A. Melsen (Andritz A/S)
P. Høgh (Andritz A/S)
J. Kiel (ECN)
F. Verhoeff (ECN)
S. Leiser (ECN)
J. Dahl (DTI)
G. Hastrup (DTI)
H.O. Hansen (DTI)
P.D. Jensen (DTI)
June 2013
ECN-L--13-041
We accept the challenge!
www.andritz.com
Brian F. Greenwood and et.al.
Key Issues in Torrefaction Process Plant Design and Operation
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
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Torrefaction of biomass can be described as a mild form of thermal conversion (controlled
carbonisation) at temperatures typically ranging between 250-300 °C in the absence of
oxygen. During torrefaction the biomass properties are changed to obtain a much better fuel
quality (increased heating value) for combustion, gasification and co-firing in conventional
coal-fired power plants and steel industry. Low calorific components are transferred to the gas
phase as water, CO2, CO and various organic acids are transferred into the gaseous phase..
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 2
The torrefaction objective is to improve the energy properties of biomass within a defined
residence time and temperature less than 300 °C.
Source ECN, Kiel et.al.
What is torrefaction?
Andritz Torrefaction Technologies
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 3
 Two Main Technology Platforms
Large plants: up to 700.000 t/a per line Small / medium plants: 50.000-250.000 t/a
Andritz/ECN Torrefaction Design Andritz ACB® Torrefaction Design*
Industrial Demoplant (1t/h) in Denmark
started up in 3rd quarter 2012
Industrial Demoplant (1t/h) in Austria in
operation from 4th quarter 2011.
Pressurized, moving bed reactor
Andritz/DTI Pelleting plant
Rotating, indirectly heated drum reactor
Briquetting plant
Key Features:
Scale up to huge capacities possible
(experience from Pulp & Paper)
Feed material: Wood Chips/Forest Residuals
Key Features:
Simple process concept specially developed for
decentralized plants
Flexibility in feed material
The ACB History and Presence
 The ACB process (ACB: Accelerated Carbonized Biomass) was developed by
an Austrian based consortium consisting of Polytechnik, Wild & Partner and
scientific support by OFI, led by Andritz AG and started in 2007.
 Development work was backed by the Austrian Research Promotion Agency
with resources from the Austrian Climate Fund.
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 4
Commissioning phase I (Drying,
Torrefaction and Energy supply)
Phase II (briquetting and storage) was
installed and started-up in September
2012.
the operation takes place continuously
3 days per week and 24 hours a day.
2011 2012 2013
Torrefaction of biomass – ACB® Process
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 5
Small capacity reactor systems for 50,000 t/a per line
Torrefaction of biomass at 250-300°C under inert conditions
• Rotating, indirectly heated drum
• Prevention of condensation problems due to gas flow pattern
• Flexibility in terms of allowable particle size
• No clogging, channeling or increase in pressure drop
• Oxygen infiltration avoided by drum sealing
technology
• Construction based on proven Drum Drying
System (> 110 such dryers worldwide)
Demo plant for production of 1 t/hr of torrefied
briquettes installed in Frohnleiten, Austria
Separation
Torrefaction of biomass
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 6
Flowsheet ACB Process
DRYING
PREPARATION
of torrefied material (milling)
DENSIFICATION
of torrefied material
Fresh biomass
Dried biomass
95% DS
Torrefied biomass
ACB gas
T=280°C
Torrefied biomass
ACB Fuel
Fresh biomass fuel
Dryer offgas
Flue gas
T=400°C
TORREFACTION
Flue gas
T=300°C
ENERGY SUPPLY
(lean gas combustion)
Separation
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
7
Andritz ACB Process, Austria
Torrefaction of biomass
Separation
Torrefaction of Biomass
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 8
Densification: Briquetting
Separation
Densification by piston press: Die diameter Ø50 mm and Ø75 mm
Max. capacity (kg/h): 1,15 t/h at die diameter of Ø75 mm
Density (w/o additives) 1,1-1,3 kg/l
Energy consumption (kWh/t) 55 kWh/t @ 1,07 t/h
Durability: up to 97%
Water uptake(5 min in water): about 1 m%
Sdr. Stenderup Torrefaction Demo Plant Project
 Andritz has built a 1 Ton/Hour Torrefaction Demo Plant in Sdr. Stenderup, Denmark
 The plant incorporates:
 Biomass (Wood Chip) Receiving
 Biomass Drying
 Torrefaction
 Pelletizing
 The plant entered commissioning in the 2nd quarter of 2012 and is currently operational.
 The project is partially funded by the Danish EUDP, (Energy Technology Development and
Demonstration Programme), with a significant majority of the capital funding from Andritz.
 The Danish Technology Institute (DTI), and energy companies Drax and Dong are involved
as part of the EUDP team.
 Energy Research Center of the Netherlands (ECN) is acting as a consultant to Andritz on
the design of the torrefaction technology and will be involved in the commissioning and
optimization of the demo plant.
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 9
10
Torrefaction Sdr. Stenderup Demo Plant
Simplified Single Line Flowsheet 1 bdmt/h wood chips
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Patents granted and Pending
ATEX Analysis was done on entire
system and multiple design
changes made.
Sdr. Stenderup Demo Plant
 The Torrefaction System:
 Blends ECN and Andritz technologies (Patents Granted and Pending)
 Pressurized for more effective heat transfer due to higher gas flows, lower
velocities and pressure drop for increased capacity .
 Provides a separation between the final drying zone and the beginning of
torrefaction
 Includes a co-current torrefaction zone
 Provides for removal of heavy organic compounds from the torrefaction gas,
minimizing plugging and deposits.
 Lends itself to scale up to large single unit capacities
 High fraction of the vessel volume is used for either final drying or reaction.
 The capacity will increase as the diameter squared.
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 11
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
12
ECN/Andritz
Pressurized Reactor Concept
Torrefaction Gas Out
to Gas Cleaning and Heating
Hot Torrefaction Gas In
Hot Torrefaction Gas In
Drying Gas In
Drying Gas Out to Heating
Wood Chips In (~8 -10% MC)
Torrefied Wood Out
Patents Granted and Pending
Sdr. Stenderup Demo Plant Overall View
PDMS used for 3D Modeling and Design
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 13
Photo April 2012
Sdr. Stenderup Torrefaction Demo Plant Project
Torrefaction reactor
during installation lift
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 14
Patents granted and Pending
Rotary Dryer
Sdr. Stenderup Torrefaction Demo Plant Project
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 15
Viewed from Feed End Viewed from Discharge End
Rotary Dryer
Sdr. Stenderup Torrefaction Demo Plant Project
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 16
Sdr. Stenderup Torrefaction Demo Plant Project
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 17
Torrefaction
Reactor Top Area
View 1
Patents granted
and Pending
Torrefaction
Reactor Process
Area
Sdr. Stenderup Torrefaction Demo Plant Project
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 18
Patents granted
and Pending
Sdr. Stenderup Torrefaction Demo Plant Project
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 19
Torrefaction
Pressurized Gas
Circulation
Blowers
Sdr. Stenderup Torrefaction Demo Plant Project
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 20
Upper Part of
Torrefied Material
Cooling Screw
and Discharge
Rotary Valve
Sdr. Stenderup Torrefaction Demo Plant Project
Pellet Press Installation
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 21
Much of the work in the last
months has been focused
around optimizing the pelleting
process.
Pellets have been produced
without using binders or
lubricants other than steam and
water for conditioning.
Specific power is higher than for
white wood pelleting.
Bulk Density > 660 kg/M3
Durability > 96 %
HHV > 21 MJ/kg
Hydrophobicity >> White Pellets
Sdr. Stenderup Torrefaction Demo Plant Project
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 22
Operating Engineer, Kristian Larsen controlling the process.
Project Status
 The plant is in operation and
producing product for test
firings and optimization.
 We are in the process of
discussing commercial scale
systems.
 We are pleased to discuss
your requirements.
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 23
Raw Materials run to Date:
Nordic Softwood Mix
Cedar
Eucalyptus
Beech
Single Pellet Tests
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 24
Laboratory scale test method to screen the pelletizing properties of
(torrefied) biomass
 Method developed and used by Danish Technological Institute - DTI
 Fast and simple method:
 Just a few grams of material are needed
 Adjustment of different pelletizing parameters i.e. Temperature,
Moisture, Particle size, Binder addition, Press channel length and
inlet design… etc.
 Information about Process & Pellet Quality
4 parameters are tested:
1. Compression of biomass
2. Static & dynamic friction
3. Pellet compression strength
4. Pellet density
Monitoring of
forces during
compression and
extrusion of pellet
from press
channel
Force required
to crush the
pellet
Single Pellet Tests
 Results give indication what parameters should be
used for pelletization
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 25
Single Pellet Tests vs. Production size mill
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 26
Good correlation between single pellet press and
production size pellet mill data
Static friction from single pellet press (N)
Energy consumption of press (kWh/t)
Self-heating of raw and torrefied biomass
 Adiabatic reactor set-up to
simulate stock-piles and storage
silos
 Materials are fed pre-dried in the
reactor in order to investigate the
impact of water uptake
 Reactor is gently purged with
air/water vapor or N2/water vapor
mixtures
 Runs with nitrogen are used as
reference cases (zero-
measurement)
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 27
Self-heating of raw and torrefied biomass
0
20
40
60
80
100
120
140
160
180
200
0 200 400 600 800 1000 1200 1400
bed
temperture
[
C]
time [min]
torrefied wood, moist air
torrefied wood, moist nitrogen
raw wood, moist air
raw wood, moist nitrogen
Water uptake
Oxidation
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 28
Self-heating of raw and torrefied biomass
0
20
40
60
80
100
120
140
160
180
200
0 200 400 600 800 1000 1200 1400
bed
temperture
[
C]
time [min]
torrefied wood, moist air
torrefied wood, moist nitrogen
raw wood, moist air
raw wood, moist nitrogen
torrefied pellets
Water uptake
Oxidation
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 29
Weathering Tests
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
Page 30
The equipment is
used to test the
effects of
the angle of
repose of the pile
of pellets and
potential flow of
moisture along the
surface layer of
the pile by
simulated Danish
rain and drying
periods under
controlled
conditions
Authors and contributors to the presentation include:
 Brian Greenwood, Bertil Stromberg and Andy Eyer (from Andritz Inc);
 Dr. Doris Thamer and Klaus Trattner (from Andritz AG);
 Allan Melsen and Peter Høgh (from Andritz A/S);
 Dr. Jaap Kiel , Dr. Fred Verhoeff and Dr. Simon Leiser (from ECN);
 Dr. Jonas Dahl, Gitte Hastrup, Hans Ove Hansen and Dr. Peter Daugbjerg
Jensen (from DTI).
 Thanks to Project Support Teams and Demo Plant Operators without whom
progress would have been much slower.
 Special thanks to all of those entities previously mentioned providing financial
support for these developments.
31 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
32 32
Thank You!
8
ECN
Westerduinweg 3 P.O. Box 1
1755 LE Petten 1755 LG Petten
The Netherlands The Netherlands
T +31 88 515 4949
F +31 88 515 8338
info@ ecn.nl
www.ecn.nl

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Torrefaction Issues

  • 1. Key Issues in Torrefaction Process Plant Design and Operation B. Greenwood (Andritz Inc) B. Stromberg (Andritz Inc) A. Eyer (Andritz Inc) D. Thamer (Andritz AG) K. Trattner (Andritz AG) A. Melsen (Andritz A/S) P. Høgh (Andritz A/S) J. Kiel (ECN) F. Verhoeff (ECN) S. Leiser (ECN) J. Dahl (DTI) G. Hastrup (DTI) H.O. Hansen (DTI) P.D. Jensen (DTI) June 2013 ECN-L--13-041
  • 2. We accept the challenge! www.andritz.com Brian F. Greenwood and et.al. Key Issues in Torrefaction Process Plant Design and Operation 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Placeholder for picture(s); the gray area must be filled COMPLETELY with one or more individual picture(s)
  • 3. Torrefaction of biomass can be described as a mild form of thermal conversion (controlled carbonisation) at temperatures typically ranging between 250-300 °C in the absence of oxygen. During torrefaction the biomass properties are changed to obtain a much better fuel quality (increased heating value) for combustion, gasification and co-firing in conventional coal-fired power plants and steel industry. Low calorific components are transferred to the gas phase as water, CO2, CO and various organic acids are transferred into the gaseous phase.. 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 2 The torrefaction objective is to improve the energy properties of biomass within a defined residence time and temperature less than 300 °C. Source ECN, Kiel et.al. What is torrefaction?
  • 4. Andritz Torrefaction Technologies 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 3  Two Main Technology Platforms Large plants: up to 700.000 t/a per line Small / medium plants: 50.000-250.000 t/a Andritz/ECN Torrefaction Design Andritz ACB® Torrefaction Design* Industrial Demoplant (1t/h) in Denmark started up in 3rd quarter 2012 Industrial Demoplant (1t/h) in Austria in operation from 4th quarter 2011. Pressurized, moving bed reactor Andritz/DTI Pelleting plant Rotating, indirectly heated drum reactor Briquetting plant Key Features: Scale up to huge capacities possible (experience from Pulp & Paper) Feed material: Wood Chips/Forest Residuals Key Features: Simple process concept specially developed for decentralized plants Flexibility in feed material
  • 5. The ACB History and Presence  The ACB process (ACB: Accelerated Carbonized Biomass) was developed by an Austrian based consortium consisting of Polytechnik, Wild & Partner and scientific support by OFI, led by Andritz AG and started in 2007.  Development work was backed by the Austrian Research Promotion Agency with resources from the Austrian Climate Fund. 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 4 Commissioning phase I (Drying, Torrefaction and Energy supply) Phase II (briquetting and storage) was installed and started-up in September 2012. the operation takes place continuously 3 days per week and 24 hours a day. 2011 2012 2013
  • 6. Torrefaction of biomass – ACB® Process 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 5 Small capacity reactor systems for 50,000 t/a per line Torrefaction of biomass at 250-300°C under inert conditions • Rotating, indirectly heated drum • Prevention of condensation problems due to gas flow pattern • Flexibility in terms of allowable particle size • No clogging, channeling or increase in pressure drop • Oxygen infiltration avoided by drum sealing technology • Construction based on proven Drum Drying System (> 110 such dryers worldwide) Demo plant for production of 1 t/hr of torrefied briquettes installed in Frohnleiten, Austria Separation
  • 7. Torrefaction of biomass 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 6 Flowsheet ACB Process DRYING PREPARATION of torrefied material (milling) DENSIFICATION of torrefied material Fresh biomass Dried biomass 95% DS Torrefied biomass ACB gas T=280°C Torrefied biomass ACB Fuel Fresh biomass fuel Dryer offgas Flue gas T=400°C TORREFACTION Flue gas T=300°C ENERGY SUPPLY (lean gas combustion) Separation
  • 8. 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 7 Andritz ACB Process, Austria Torrefaction of biomass Separation
  • 9. Torrefaction of Biomass 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 8 Densification: Briquetting Separation Densification by piston press: Die diameter Ø50 mm and Ø75 mm Max. capacity (kg/h): 1,15 t/h at die diameter of Ø75 mm Density (w/o additives) 1,1-1,3 kg/l Energy consumption (kWh/t) 55 kWh/t @ 1,07 t/h Durability: up to 97% Water uptake(5 min in water): about 1 m%
  • 10. Sdr. Stenderup Torrefaction Demo Plant Project  Andritz has built a 1 Ton/Hour Torrefaction Demo Plant in Sdr. Stenderup, Denmark  The plant incorporates:  Biomass (Wood Chip) Receiving  Biomass Drying  Torrefaction  Pelletizing  The plant entered commissioning in the 2nd quarter of 2012 and is currently operational.  The project is partially funded by the Danish EUDP, (Energy Technology Development and Demonstration Programme), with a significant majority of the capital funding from Andritz.  The Danish Technology Institute (DTI), and energy companies Drax and Dong are involved as part of the EUDP team.  Energy Research Center of the Netherlands (ECN) is acting as a consultant to Andritz on the design of the torrefaction technology and will be involved in the commissioning and optimization of the demo plant. 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 9
  • 11. 10 Torrefaction Sdr. Stenderup Demo Plant Simplified Single Line Flowsheet 1 bdmt/h wood chips 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Patents granted and Pending ATEX Analysis was done on entire system and multiple design changes made.
  • 12. Sdr. Stenderup Demo Plant  The Torrefaction System:  Blends ECN and Andritz technologies (Patents Granted and Pending)  Pressurized for more effective heat transfer due to higher gas flows, lower velocities and pressure drop for increased capacity .  Provides a separation between the final drying zone and the beginning of torrefaction  Includes a co-current torrefaction zone  Provides for removal of heavy organic compounds from the torrefaction gas, minimizing plugging and deposits.  Lends itself to scale up to large single unit capacities  High fraction of the vessel volume is used for either final drying or reaction.  The capacity will increase as the diameter squared. 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 11
  • 13. 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 12 ECN/Andritz Pressurized Reactor Concept Torrefaction Gas Out to Gas Cleaning and Heating Hot Torrefaction Gas In Hot Torrefaction Gas In Drying Gas In Drying Gas Out to Heating Wood Chips In (~8 -10% MC) Torrefied Wood Out Patents Granted and Pending
  • 14. Sdr. Stenderup Demo Plant Overall View PDMS used for 3D Modeling and Design 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 13
  • 15. Photo April 2012 Sdr. Stenderup Torrefaction Demo Plant Project Torrefaction reactor during installation lift 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 14 Patents granted and Pending
  • 16. Rotary Dryer Sdr. Stenderup Torrefaction Demo Plant Project 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 15 Viewed from Feed End Viewed from Discharge End
  • 17. Rotary Dryer Sdr. Stenderup Torrefaction Demo Plant Project 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 16
  • 18. Sdr. Stenderup Torrefaction Demo Plant Project 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 17 Torrefaction Reactor Top Area View 1 Patents granted and Pending
  • 19. Torrefaction Reactor Process Area Sdr. Stenderup Torrefaction Demo Plant Project 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 18 Patents granted and Pending
  • 20. Sdr. Stenderup Torrefaction Demo Plant Project 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 19 Torrefaction Pressurized Gas Circulation Blowers
  • 21. Sdr. Stenderup Torrefaction Demo Plant Project 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 20 Upper Part of Torrefied Material Cooling Screw and Discharge Rotary Valve
  • 22. Sdr. Stenderup Torrefaction Demo Plant Project Pellet Press Installation 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 21 Much of the work in the last months has been focused around optimizing the pelleting process. Pellets have been produced without using binders or lubricants other than steam and water for conditioning. Specific power is higher than for white wood pelleting. Bulk Density > 660 kg/M3 Durability > 96 % HHV > 21 MJ/kg Hydrophobicity >> White Pellets
  • 23. Sdr. Stenderup Torrefaction Demo Plant Project 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 22 Operating Engineer, Kristian Larsen controlling the process.
  • 24. Project Status  The plant is in operation and producing product for test firings and optimization.  We are in the process of discussing commercial scale systems.  We are pleased to discuss your requirements. 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 23 Raw Materials run to Date: Nordic Softwood Mix Cedar Eucalyptus Beech
  • 25. Single Pellet Tests 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 24 Laboratory scale test method to screen the pelletizing properties of (torrefied) biomass  Method developed and used by Danish Technological Institute - DTI  Fast and simple method:  Just a few grams of material are needed  Adjustment of different pelletizing parameters i.e. Temperature, Moisture, Particle size, Binder addition, Press channel length and inlet design… etc.  Information about Process & Pellet Quality
  • 26. 4 parameters are tested: 1. Compression of biomass 2. Static & dynamic friction 3. Pellet compression strength 4. Pellet density Monitoring of forces during compression and extrusion of pellet from press channel Force required to crush the pellet Single Pellet Tests  Results give indication what parameters should be used for pelletization 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 25
  • 27. Single Pellet Tests vs. Production size mill 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 26 Good correlation between single pellet press and production size pellet mill data Static friction from single pellet press (N) Energy consumption of press (kWh/t)
  • 28. Self-heating of raw and torrefied biomass  Adiabatic reactor set-up to simulate stock-piles and storage silos  Materials are fed pre-dried in the reactor in order to investigate the impact of water uptake  Reactor is gently purged with air/water vapor or N2/water vapor mixtures  Runs with nitrogen are used as reference cases (zero- measurement) 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 27
  • 29. Self-heating of raw and torrefied biomass 0 20 40 60 80 100 120 140 160 180 200 0 200 400 600 800 1000 1200 1400 bed temperture [ C] time [min] torrefied wood, moist air torrefied wood, moist nitrogen raw wood, moist air raw wood, moist nitrogen Water uptake Oxidation 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 28
  • 30. Self-heating of raw and torrefied biomass 0 20 40 60 80 100 120 140 160 180 200 0 200 400 600 800 1000 1200 1400 bed temperture [ C] time [min] torrefied wood, moist air torrefied wood, moist nitrogen raw wood, moist air raw wood, moist nitrogen torrefied pellets Water uptake Oxidation 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 29
  • 31. Weathering Tests 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 Page 30 The equipment is used to test the effects of the angle of repose of the pile of pellets and potential flow of moisture along the surface layer of the pile by simulated Danish rain and drying periods under controlled conditions
  • 32. Authors and contributors to the presentation include:  Brian Greenwood, Bertil Stromberg and Andy Eyer (from Andritz Inc);  Dr. Doris Thamer and Klaus Trattner (from Andritz AG);  Allan Melsen and Peter Høgh (from Andritz A/S);  Dr. Jaap Kiel , Dr. Fred Verhoeff and Dr. Simon Leiser (from ECN);  Dr. Jonas Dahl, Gitte Hastrup, Hans Ove Hansen and Dr. Peter Daugbjerg Jensen (from DTI).  Thanks to Project Support Teams and Demo Plant Operators without whom progress would have been much slower.  Special thanks to all of those entities previously mentioned providing financial support for these developments. 31 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2
  • 33. 21st European Biomass Conference and Exhibition: Session Reference: 4AO.8.2 32 32 Thank You!
  • 34. 8 ECN Westerduinweg 3 P.O. Box 1 1755 LE Petten 1755 LG Petten The Netherlands The Netherlands T +31 88 515 4949 F +31 88 515 8338 info@ ecn.nl www.ecn.nl