impact of biodiesel-based na on the selective catalytic ... · field pennycress, jatropha, etc. –...
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Impact of Biodiesel-Based Na
on the Selective Catalytic Reduction (SCR) of NOx Using
Cu-zeolite D. William Brookshear1,
Todd J. Toops2, William Rohr1, Ke Nguyen1, and Bruce G. Bunting2
1-University of Tennessee - Knoxville
2-Oak Ridge National Laboratory
2011 DEER Conference
October 5, 2011
2 Managed by UT-Battelle for the U.S. Department of Energy
Motivation to introduce higher levels of biodiesel tempered by the unknown • Biodiesel: alkyl ester combusts similar to diesel fuel
• Domestic renewable energy source synthesized from
vegetable oil or animal fat – Vegetable: Soybean (~90%), rapeseed,
field pennycress, jatropha, etc. – Animal sources: Only waste or by-products being
converted at this time – Currently focus is on waste/excess oil
• Barrier to implementation is the unknowns associated
with a new fuel – Combusts like diesel, but unknown impact on
emissions control devices – Trace elements are primary cause of concern in
emissions control…particularly Na and K
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Concerns associated with Na and K are mechanical and chemical
• NaOH or KOH is a liquid-phase catalyst used in biodiesel synthesis – NaOH and KOH difficult to separate
completely from products – Specification set at 5 ppm Na+K in
B100
• Potential Na/K emissions control effects – Ash accumulation in DPF – Alkali absorption into monolith walls
• possible weakening of monolith – Catalyst poisoning/fouling
• Na-exchanged zeolite is commercial catalyst
Migration into cordierite
Increased ash accumulation
NaOH or
KOH biodiesel
Vegetable oil +
methanol
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Recent research illustrates potential Na impact on SCR and DPF cordierite walls • Cavataio et al. (SAE 2009-01-2823) • Aqueous addition of Na to SCR and
DOC using incipient wetness technique – Investigated Na and K – Multiple DOC and SCR formulations
• Dramatic deactivation observed • Na and K accelerated zeolite structure
collapse
• Williams et al. (SAE 2011-01-1136) • Accelerated full-size engine approach
– DOCDPFSCR approach – Both Na and K added to fuel – 150k and 435k mile equivalent
• Na+K penetrate wall of DPF • Small but significant decrease in NOx
performance
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Accelerated aging targets Na-impact
• Introduce high levels of Na to B20
• Two configurations evaluated – DOCSCRDPF
• “light duty” configuration • with and without Na (control)
– DOCDPFSCR • “heavy duty” configuration
• Levels elevated to achieve 435,000 mile Na exposure
– Dioctyl sulfo-succinate sodium salt with Na:S = 1 – 5000+ ppm Na in B20 – Periodic soot regeneration performed at 700°C – Measure performance in bench-core reactor
• First 3” of catalysts studied • Employ portions of the CLEERS SCR protocol • SV = 30,000 h-1, NH3/NO = 0.8-1.0, NO2:NO = 0 or 1
DOC
Mix
erSCRDP
F
DOC
Mix
erSCRDP
F
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DOC-SCR-DPF (LIGHT-DUTY)
Na ACCELERATED-AGING
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Na observed after accelerated aging throughout SCR washcoat • Na throughout washcoat
– In bulk ~0.2%wt • Elevated Na levels also
observed at surface – 0.3-0.6%wt
• Concentration of Na axially
uniform
• Low sulfur levels detected in SCR washcoat – Near detection limit – Increased level at
surface ~0.1%wt – Na:S ≠ 1
Accelerated Na-Aged SCR (from DOCSCRDPF) Inlet (center) Inlet (near edge) Middle
Na
200 μm
EPMA line scans
0.00.10.20.30.40.50.6
0% 20% 40% 60% 80% 100%Fraction from monolith to surface
Ato
mic
Wei
gh
t % Na in Front Na in Middle
S in Front S in Middle
120 μm
20
0
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A version of the CLEERS transient SCR protocol utilized to probe behavior
cool
0 20 40 60 80 100 120 140 160
time (minutes)
T
O2
NH3
NO
NO2
Ti
0%
350
0
350
0
350
0
14%
NH3 uptake
NO+NO2 SCR
NO SCR α = 0.9 0.8 1.0
NO oxidation cool
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Standard SCR reaction significantly inhibited with Na addition • Some aging observed for both the control and Na addition
– Illustrates some thermal effects on this model Cu zeolite SCR catalyst • SCR with Na has significantly less activity for the standard SCR reaction
0102030405060708090
100
150 250 350 450 550
NO
xCo
nver
sion
(%)
Temperature (°C)
Standard Reaction (NO2:NO = 0:1)
Fresh
Control (w/o Na)
DOC-SCR-DPF w/ Na
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Minimal impact when feeding equimolar NO2:NO (fast SCR reaction) • Minimal effects when feeding both NO2 and NO
– However, the catalyst most affected is the SCR with Na addition
0
20
40
60
80
100
150 250 350 450 550
NO
xCo
nver
sion
(%)
Temperature (°C)
Fast SCR reaction NO:NO2 = 1:1
Fresh
Control (w/o Na)
DOC-SCR-DPF w/ Na
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NH3 storage decreases with aging; control and Na-aged show similar impact
• Significant impact on NH3 storage for both aged samples – Similar impact suggests thermal effect is more responsible than Na
0
0.02
0.04
0.06
0.08
0.1
0.12
0.14
0.16
150 250 350 450 550
NH
3 St
orag
e (m
mol
/gca
t)
Temperature (°C)
NH3 Storage
Fresh
Control (w/o Na)
DOC-SCR-DPF w/ Na
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NH3 oxidation decreases with aging • NH3 oxidation reduced above 400°C in both aged samples
– Oxidation associated with Cu sites – Significant difference between control and Na-aged SCR suggests Na effect
0
10
20
30
40
50
60
70
80
150 250 350 450 550
Oxi
dati
on -
%
Temperature (°C)
NH3 Oxidation
Fresh
Control (w/o Na)
DOC-SCR-DPF w/ Na
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Further evidence of Na impact on Cu-sites with decreased NO oxidation • Na-aged samples show less oxidation of NO to NO2 over entire
temperature range • Fresh and control show similar, albeit low reactivity
0
1
2
3
4
5
6
150 250 350 450 550
%N
O O
xidi
zed
to N
O2
Temperature (°C)
NO Oxidation
Fresh
Control (w/o Na)
DOC-SCR-DPF w/ Na
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Increasing NH3 does not improve performance on Na-aged SCR • Indicates NH3 oxidation does not limit
performance – NH3 breakthrough observed
• Further illustrates NO to NO2 oxidation is limiting performance in Na-aged sample – Oxidation sites are most impacted
• Impact on control is less pronounced
0 10 20 30 40 50 60 70 80 90
100
150 250 350 450 550
NO
x Co
nver
sion
(%)
Temperature ( C)
Na-addition, NO2:NO = 0:1
Alpha = 1.0
Alpha = 0.9
Alpha = 0.8
0 10 20 30 40 50 60 70 80 90
100
150 250 350 450 550
NO
x Co
nver
sion
(%)
Temperature ( C)
Control (w/o Na), NO2:NO = 0:1
Alpha = 1.0
Alpha = 0.9
Alpha = 0.8
0 10 20 30 40 50 60 70 80 90
100
150 250 350 450 550
NO
x Co
nver
sion
(%)
Temperature ( C)
Fresh, NO2:NO = 0:1
Alpha = 1.0
Alpha = 0.9
Alpha = 0.8
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Control-SCR and Na-aged SCR have similar BET profiles
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DOC DPF SCR
(HEAVY-DUTY) Na ACCELERATED-AGING
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Minimal Na Contamination SCR when placed after DPF
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When DPF is in front of SCR, catalyst is protected from Na and its effects • No significant effect from accelerated Na-aging if DPF is in front of SCR
– Some protection from thermal effects also gained with DPF upstream of SCR
0102030405060708090
100
150 250 350 450 550
NO
xCo
nver
sion
(%)
Temperature (°C)
Standard Reaction (NO2:NO = 0:1)
FreshControl (w/o Na)DOC-SCR-DPF w/ NaDOC-DPF-SCR w/ Na
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Similar good behavior observed with fast SCR conditions
0
20
40
60
80
100
150 250 350 450 550
NO
xCo
nver
sion
(%)
Temperature (°C)
Fast SCR reaction NO:NO2 = 1:1
FreshControl (w/o Na)DOC-SCR-DPF w/ NaDOC-DPF-SCR w/ Na
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NH3 storage similar to that of fresh SCR • No aging or Na contamination impact on NH3 storage capability of catalyst
– DPF upstream of SCR preserves storage capability of catalyst
0
0.02
0.04
0.06
0.08
0.1
0.12
0.14
0.16
150 250 350 450 550
NH
3 St
orag
e (m
mol
/gca
t)
Temperature (°C)
NH3 Storage
Fresh
Control (w/o Na)
DOC-SCR-DPF w/ Na
DOC-DPF-SCR w/ Na
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NO and NH3 oxidation were similarly less affected
• NH3 oxidation only slightly lower than that of fresh SCR • NO to NO2 oxidation shows moderately higher oxidation activity
0
10
20
30
40
50
60
70
80
150 250 350 450 550
Oxi
dati
on -
%
Temperature (°C)
NH3 Oxidation
FreshControl (w/o Na)DOC-SCR-DPF w/ NaDOC-DPF-SCR w/ Na
0
1
2
3
4
5
6
7
150 250 350 450 550
%N
O O
xidi
zed
to N
O2
Temperature (°C)
NO Oxidation
FreshControl (w/o Na)DOC-SCR-DPF w/ NaDOC-DPF-SCR w/ Na
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BET Surface Area Analysis of SCRs • SCR from DOC-SCR-DPF configuration shows highest surface area
reduction, while SCR from DOC-DPF-SCR configuration is unaffected
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Future Directions • Does ASTM specification need to be lowered? If so what level?
– NREL lead collaboration • Focus of NREL/MECA/Ford/ORNL/NBB collaboration
– Ford F250 with full emissions control system – 150,00 mile equivalent with ULSD, Na, K, and Ca – Light Duty (DOC-SCR-DPF) results forthcoming
• Systematic study of Na impact on mechanical strength of DPF walls – Funded through the Advanced Propulsions Materials Program (Jerry Gibbs) – Collaboration with Michael Lance and Andy Wereszczak
• ORNL – Materials Science and Technology Division • Strength testing technique discussed at poster Tuesday night (P-15)
– Long term aging approach with overnight operation
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Summary • Na can significantly impact the chemistry
of SCR catalysis
• When placed behind a DPF the impact is significantly muted
• Impact of both thermal and Na
contamination less severe when feeding equimolar amounts of NO and NO2
• Results discussed in bonus slides – Na contamination in accelerated aged
samples mimics that seen in long-term engine aged catalysts
– Na penetrates cordierite walls of DPF
• Manuscript submitted to Catalysis Today (under review)
Na 16
0 200 μm
0102030405060708090
100
150 250 350 450 550
NO
xCo
nver
sion
(%)
Temperature (°C)
Standard Reaction (NO2:NO = 0:1)
FreshControl (w/o Na)DOC-SCR-DPF w/ NaDOC-DPF-SCR w/ Na
0
20
40
60
80
100
150 250 350 450 550
NO
xCo
nver
sion
(%)
Temperature (°C)
Fast SCR reaction NO:NO2 = 1:1
FreshControl (w/o Na)DOC-SCR-DPF w/ NaDOC-DPF-SCR w/ Na
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Acknowledgements
• Funding provided by DOE – Vehicles Technology Program – Kevin Stork: Fuels & Lubricants – Non-Petroleum Based Fuels
• Long-term aged emissions control parts
– General Motors – Umicore, MECA
• Discussions and project development
– Bob McCormick, Matt Thornton, Aaron Williams – NREL – Rasto Brezny – MECA
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Additional slides
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COMPARISON OF ACCELERATED APPROACH
TO LONG-TERM AGING
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Long-term engine-aged systems used for comparison when possible
B20 DOC DPF • Obtained from GM
– Pt/Al2O3-based DOC – SiC-based DPF
• Field-aged system with B20 – 120,000 mile equivalent
• Minimal knowledge about aging details – Na content was below specification
• Exact value unknown – Temperature history unknown
• Unfortunately unable to secure any B20-
aged SCR catalysts
DPF section
DOC
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Biodiesel and lube oil components observed in DOC; accelerated- and engine-aged results similar
• Na, S and P observed in DOC – Inlet cross-sections shown with EPMA
• Long–term aged – S throughout washcoat – P at surface of washcoat – Na observed at surface
• Primarily at inlet of DOC • Accelerated aged
– S throughout washcoat – Minimal lube oil phosphorous detected – Na observed throughout DOC
• Equally in inlet and exit of DOC
Long-term aged DOC Accelerated-aged DOC 10
0 200 μm
S
15
0
P
200 μm
Na 16
0 200 μm
Long-term Aging Accelerated Aging
Average Maximum Penetration Average Maximum Penetration
S 0.70% 1.00% throughout 0.40% 0.60% throughout
P n/a 8% 30 μm n/a <0.1% <10 μm
Na n/a 0.40% 30 μm n/a 0.40% 30 μm
15
15
45
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DOC minimally affected; similar effects shown for both accelerated- and engine-aged devices
• Both aged samples show slight decrease between 225°C and 300°C – Conversion decreases by <12%
• Oxidation of NO to NO2 is as much as
12% higher in engine-aged DOC samples than in fresh – This effect is possibly due to
increased Pt particle size from thermal aging, which can improve NO to NO2 oxidation
0102030405060708090
100
100 200 300 400
NO
Oxi
dati
on -
%
Temperature - C
NO to NO2 Oxidation in DOC
FreshAccelerated Na-AgedEngine-Aged
0102030405060708090
100
100 200 300 400
Ethy
lene
Con
vers
ion
-%
Temperature - C
Ethylene Conversion in DOC
FreshAccelerated Na-AgedEngine-Aged
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EPMA ANALYSIS OF DPF SAMPLES
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• DOC-SCR-DPF: penetration is observed; not deep
Back of DPF Middle of DPF Front of DPF
Na found in walls of cordierite DPFs N
a EP
MA
Ba
ck S
catt
er Im
ages
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Back of DPF Middle of DPF Front of DPF N
a EP
MA
Ba
ck S
catt
er Im
ages
Na found in walls of cordierite DPFs • DOC-DPF-SCR: penetration is more severe; closer to DOC exotherm
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Ash in long-term GM-aged DPFs (SiC) • Ash plugs apparent in rear of DPF • 20x more Ca than Na detected in
ash – Ca associated with standard
lube oil • Na not detected in wall of SiC DPF
FLOW FLOW
Ash plugs in exposed DPF channels
Ca Na
P S
EPMA of ash plugs in DPF