biomass and coal characteristics: implications for cofiring
DESCRIPTION
Biomass and Coal Characteristics: Implications for Cofiring. David A. Tillman Foster Wheeler Power Group, Inc. Clinton, NJ . Abstract. Fuel Characterization Research at The Energy Institute of Pennsylvania State University Proximate and Ultimate Analysis - PowerPoint PPT PresentationTRANSCRIPT
Biomass and Coal Characteristics: Implications
for Cofiring
David A. Tillman
Foster Wheeler Power Group, Inc.
Clinton, NJ
AbstractWoody and herbaceous biomass fuels exhibit distinct and separate characteristics with respect to bulk chemistry and behavior; further these fuels are fundamentally different from the various coals used in power generation. Detailed characterization of sawdust, urban wood waste, fresh switchgrass, and weathered switchgrass demonstrates the critical—and sometimes subtle—differences between these fuels. Critical among these differences is fuel reactivity measured both in maximum volatile yield and rate of fuel devolatilization. Of additional importance is the reactivity of the fuel nitrogen in the various biomass fuels. Detailed characterization of fuels demonstrates the fundamental differences in combustion characteristics between the various biomass fuels and the various coals burned in utility power plants. These differences can be used to explain the outcomes of cofiring in pulverized coal boilers—particularly the potential for simultaneous reduction of NOx, unburned carbon in flyash, and CO emissions. Using drop tube furnace data developed by The Energy Institute of The Pennsylvania State University, and field data from various biomass cofiring projects, this paper uses the detailed fuel characteristics to identify critical combustion mechanisms occurring during cofiring of various biomass fuels and coal in pulverized coal boilers.
Basis of the Analysis• Fuel Characterization Research at The Energy
Institute of Pennsylvania State University– Proximate and Ultimate Analysis– Drop Tube Reactor Testing (400 – 1700oC)
» Determine maximum volatile release» Determine fuel reactivity» Determine nitrogen and carbon volatile
release– 13C NMR Testing
• Develop Relationships to Full Scale Cofiring Testing
Focus of the PSU Research
• Nitrogen Evolution from Solid Fuels Governs NOx Formation from Fuel Nitrogen
– NOx Control is Favored by Volatile Nitrogen
– NOx Control is Favored by Nitrogen Rapidly Evolving from the Fuel Mass
• Understanding Nitrogen Evolution Patterns can Assist in Explaining NOx Reduction with Biomass and Low Rank Coals
• Understanding Nitrogen Evolution Patterns for a Given Suite of Fuels can Influence Fuel Selection
Support for this Research• USDOE – NETL and USDOE – EERE in
Sponsoring Biomass Cofiring Technology Assessment
• USDOE – NETL, USDOE – EERE, and EPRI in Sponsoring Cofiring Research and Demonstration Projects with a Variety of Coals in Cyclone and PC Boilers
– Albright Station, Willow Island Station– Bailly Station, Michigan City Station– Seward Station, Shawville Station– Allen Fossil Plant, Colbert Fossil Plant
Background: Previous Studies
• Baxter et. al., 1995. Seminal Paper on Nitrogen Evolution from Coals as a Function of Residence Time
• Research for USDOE and EPRI, Sponsored by USDOE and Performed by The Energy Institute of Pennsylvania State University and by Foster Wheeler Power Group, Inc.
Methodology - 1• Select Representative Biomass Fuels
– Sawdust– Urban Wood Waste– Fresh Switchgrass– Weathered Switchgrass
• Basis of Selection– Commonly used in cofiring applications– Represent woody and herbaceous biomass
• Select Reference Coals– Black Thunder [PRB]– Pittsburgh #8
Methodology - 2
• Sawdust source: West Virginia [Willow Island Cofiring Project]
• Urban Wood Waste source: produced from a blend of plywood, particleboard, and paneling to be highly similar to the urban wood waste at Bailly Generating Station, with particular attention to nitrogen content
• Weathered Switchgrass source: Gadsden, Alabama [Southern Co. and Southern Research Institute Cofiring Project]
• Fresh Switchgrass source: Southern Co. and Auburn University
Methodology - 3• Characterize the Incoming Fuel
– Proximate and Ultimate Analysis– Heating Value
• Air Dry and Grind Fuel• Pyrolyze Fuel in Drop Tube Reactor (DTR)
– 400oC – 1700oC– Argon Environment
• Determine Distribution of Nitrogen in Incoming Fuel (volatile N vs char N)
• Determine Nitrogen, Carbon, and Total Volatile Evolution as a Function of Temperature
Methodology - 4• Basic Premise:
If nitrogen is in volatile form, and if nitrogen volatiles evolve more rapidly than carbon volatiles or total volatile matter, then NOx formation is more easily controlled by combustion mechanisms
If nitrogen is in char form, or if nitrogen volatile evolution lags behind carbon volatile evolution or total volatile evolution, then NOx formation control by combustion mechanisms is more difficult and less effective
Analysis of Biomass Fuels Parameter Fuel Fresh
Mixed Sawdust
Urban Wood Waste
Fresh Switchgrass
Weathered Switchgrass
Proximate Analysis (wt % dry basis) Volatiles 80.0 76.0 76.18 80.93
Fixed Carbon 19.0 18.1 16.08 18.34 Ash 1.0 5.9 7.74 0.73
Ultimate Analysis (wt % dry basis) Carbon 49.2 48.0 46.73 51.44
Hydrogen 6.0 5.5 5.88 5.97 Nitrogen 0.3 1.4 0.54 1.45
Sulfur <0.1 0.1 0.13 0.04 Oxygen 43.0 39.1 38.99 40.36
Ash 1.0 5.9 7.74 0.73 HHV (Btu/lb) 8400 8364 7750 8150
Distribution of Fuel Nitrogen
0
0.2
0.4
0.6
0.8
1
1.2
1.4
1.6
1.8
Distribution of Fuel Nitrogen by Type (lb/MMBtu)
Urban wood Fresh Weathered Black Pittsburgh
Sawdust Waste Switchgrass Switchgrass Thunder #8
Fuel Type
Volatile Fuel Nitrogen
Volatile Fuel Nitrogen (light green)
Char Fuel Nitrogen (dark green)
Maximum Volatile Nitrogen Yield
0.00%
10.00%
20.00%
30.00%
40.00%
50.00%
60.00%
70.00%
80.00%
90.00%
100.00%
Maximum Nitrogen Volatile
Yield (%)
Urban wood Fresh Weathered Black Pittsburgh
Sawdust Waste Switchgrass Switchgrass Thunder #8
Fuel Type
Sawdust Nitrogen and Carbon Volatile Yields
0.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
80.00
90.00
100.00
0 200 400 600 800 1000 1200 1400 1600 1800
Temperature (C)
Perc
en
t C
arb
on
or
Nit
rog
en
in
Vo
lati
le M
att
er
Carbon
Nitrogen
Sawdust Nitrogen and Carbon Evolution Normalized to Total Volatile Matter
Evolution
0.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
80.00
90.00
100.00
0.0% 10.0% 20.0% 30.0% 40.0% 50.0% 60.0% 70.0% 80.0% 90.0% 100.0%
Percent Volatile Matter Evolved
Pe
rce
nt
Nit
rog
en
or
Ca
rbo
n
Ev
olv
ed
as
Vo
lati
les
Nitrogen Volatiiles Formed
Carbon Volatiles Formed
Nitrogen and Carbon Volatile Evolution from Urban Wood Waste
0.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
80.00
90.00
100.00
0 200 400 600 800 1000 1200 1400 1600 1800
Temperature (C)
Vo
lati
le Y
ield
of
Car
bo
n a
nd
Nit
rog
en
Nitrogen
Carbon
Nitrogen and Carbon Volatile Evolution from Fresh Switchgrass
0.00
10.00
20.00
30.00
40.00
50.00
60.00
70.00
80.00
90.00
100.00
0 200 400 600 800 1000 1200 1400 1600 1800
Temperature (C)
Per
cen
t C
arb
on
or
Nit
rog
en V
ola
tili
zed
Nitrogen
Carbon
Nitrogen and Carbon Volatile Evolution from Weathered Switchgrass
0.00%
10.00%
20.00%
30.00%
40.00%
50.00%
60.00%
70.00%
80.00%
90.00%
100.00%
0 200 400 600 800 1000 1200 1400 1600 1800
Temperature (C)
Vo
lati
le Y
ield
of
Car
bo
n o
r N
itro
gen
Nitrogen
Carbon
Nitrogen and Carbon Volatile Evolution from Weathered Switchgrass Normalized
to Total Volatile Evolution
0.00%
10.00%
20.00%
30.00%
40.00%
50.00%
60.00%
70.00%
80.00%
90.00%
100.00%
0.0% 10.0% 20.0% 30.0% 40.0% 50.0% 60.0% 70.0% 80.0% 90.0% 100.0%
Percent Total Volatile Yield From Fuel
Pe
rce
nt
Ev
olv
ing
as
Vo
lati
le M
att
er
Nitrogen Volatile Yield
Carbon Volatile Yield
Nitrogen and Carbon Evolution from Black Thunder PRB Coal
0.00%
10.00%
20.00%
30.00%
40.00%
50.00%
60.00%
70.00%
80.00%
90.00%
0 200 400 600 800 1000 1200 1400 1600 1800
Temperature (C)
Per
cen
t V
ola
tili
zed
Nitrogen Carbon
Total Fuel
Nitrogen and Carbon Volatile Evolution from Pittsburgh #8 Coal
0.00%
10.00%
20.00%
30.00%
40.00%
50.00%
60.00%
70.00%
80.00%
0 200 400 600 800 1000 1200 1400 1600 1800
Temperature (C)
Pe
rce
nt
of
Ele
me
nt
Ev
olv
ed
as
Vo
lati
le M
att
er
Percent Nitrogen Evolved as Volatile Matter
Percent Carbon Evolved as Volatile Matter
Nitrogen and Carbon Volatile Evolution from Pittsburgh #8 Coal Normalized to
Total Volatile Yield
0
10
20
30
40
50
60
70
80
90
100
0.0% 10.0% 20.0% 30.0% 40.0% 50.0% 60.0% 70.0% 80.0% 90.0% 100.0%
Percent Total Volatile Matter Evolved
Pe
rce
nt
Ca
rbo
n a
nd
Nit
rog
en
Ev
olv
ed
as
V
ola
tile
Ma
tte
r
Nitrogen/Carbon Atomic Ratios in Char Normalized to N/C Ratio in Initial Fuel
0
0.5
1
1.5
2
2.5
0 200 400 600 800 1000 1200 1400 1600 1800
Temperature (C)
No
rmal
ized
N/C
Ato
mic
Rat
io in
So
lid F
uel
an
d
Ch
ar
Fresh Sawdust
Weathered Switchgrass
Black Thunder
Urban Wood Waste
Pittsburgh #8
Fresh Switchgrass
NOx Reductions at Albright
0
0.1
0.2
0.3
0.4
0.5
0.6
0.00 2.00 4.00 6.00 8.00 10.00 12.00
Cofiring Percentage, Mass Basis
NO
x E
mis
sio
ns,
lb
/MM
Btu
NOx Reductions at Albright (2)
• NOx = 0.361 – 0.0043(Cm) + 0.022(EO2) – 0.00055(SOFA)
• Definitions:– Cm is cofiring percentage, mass basis [0 – 10]
– EO2 is excess O2 at furnace exit (wet basis) [1 – 4]
– SOFA is separated overfire air damper positions for all 3 levels [0 – 240]
• r2 = 0.87, 68 observations• Probabilities of random occurrence: equation,
4.2x10-28; intercept, 2.3x10-24; Cm, 1.2x10-5; EO2, 5.9x10-4; SOFA, 5.0x10-22
NOx Reduction at Seward Station
y = 0.0004x2 - 0.0034x + 0.0657
R2 = 0.8507
0.00%
2.00%
4.00%
6.00%
8.00%
10.00%
12.00%
14.00%
16.00%
18.00%
20.00%
0 5 10 15 20 25
Sawdust Cofiring Percentage, Mass Basis
NO
x R
ed
ucti
on
Perc
en
tag
e
NOx Reduction at all EPRI Demos
Average NOx Emissions Reduction
0
5
10
15
20
25
30
0 2 4 6 8 10 12
Percent Cofiring, Btu Basis
Pe
rce
nt
NO
x R
ed
uc
tio
n f
rom
Te
st
Ba
se
lin
e
Line Indicates 1% NOx Reduction for Every 1% Cofiring Percentage (Btu Basis)
Conclusions• Fuel reactivity is a key to NOx control using
staged combustion
• Biomass fuels, in general, are highly reactive although weathering reduces nitrogen reactivity in switchgrass
• The relative reactivity of biomass, and various coals, can be used as a technique to evaluate potential in NOx management
• The DTR technique for analyzing fuels has significant benefits in evaluating initial combustion processes applied to NOx management