Low Temperature Emission Control · 16/05/2013 · • emissions standards harder to meet, getting...
Transcript of Low Temperature Emission Control · 16/05/2013 · • emissions standards harder to meet, getting...
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Low Temperature Emissions Control
Todd J. Toops (co-Principal Investigator) James E. Parks (co-Principal Investigator) J. Chris Bauer Oak Ridge National Laboratory Energy and Transportation Science Division
ACE085 May 16, 2013
This presentation does not contain any proprietary, confidential, or otherwise restricted information
Gurpreet Singh and Ken Howden Advanced Combustion Engine Program
U.S. Department of Energy
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Project Overview
• Started in FY2013 − Reprogrammed project that was
unfunded in 2012 − Prior project focused on effects of
advanced combustion regimes on emissions control (Multi-mode)
Timeline Barriers
Budget • FY2013: $400k (expected) • FY2012: $0k
• BES-funded scientists Sheng Dai and Steve Overbury
• Center for Nanophase Materials Science (CNMS) user project
• From DOE Vehicle Technologies Multi-Year Program Plan (2011-2015) − 2.3.1.B: Lack of cost-effective
emission control − 2.3.1.D: Durability
• Responsive to ACEC Tech Team requested emphasis on low temperature emissions control Partners
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Objectives and Relevance Develop emission control technologies that perform at low temperatures (<150ºC) to
enable fuel-efficient engines with low exhaust temperatures to meet emission regulations
Top: J.Kubsh, “Light-duty Vehicle Emission Standards”, 01/10/2013. Bottom: C. DiMaggio, “ACEC Low Temperature Aftertreatment Program”, 06/21/2012.
Emissions
Fuel
Econ
omy
• Project aims to identify advancements in technologies that will enable commercialization of advanced combustion engine vehicles
– Advanced combustion engines have greater efficiency needed to meet CAFE • consequently lower exhaust temperatures
– At low temperatures catalysis is challenging • emissions standards harder to meet, getting stricter
• Perform research on strategies to improve low temperature catalysis for emission control
– Need ~90% conversion at T ≤ 150°C
• Investigate “trap” material technologies that would temporarily store emissions
– Released and converted later under periodic high temperature conditions
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Improved vehicle efficiency leads to low exhaust temperature • Advanced combustion modes have greater
efficiency and consequently lower exhaust temperatures
• Low temperature exhaust is not simply a start-up problem
• Exhaust temperatures stay low throughout the FTP
• Further improvements in efficiency will be even more challenging for emissions
– Waste heat recovery (WHR) – ACEC: “Turbo = Catalyst Refrigerator”
Top: C. Lambert, “Future Directions in SCR Systems”, 2012 CLEERS workshop, 05/01/2012. Bottom: M. Zammitt, “ACEC Future Aftertreatment Strategy Report”, 01/10/2012. Turbo: http://www.autoblog.com/2012/10/03/turbo-sales-to-accelerate-by-80-could-make-up-40-of-global-of/
=
TURBOTurbo
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Current emissions control technologies have limited activity at 150°C
TWC
All: M. Zammitt, “ACEC Future Aftertreatment Strategy Report”, 01/10/2012.
DOC (HC)
LNT
SCR
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Approach: Pursue innovative catalyst technologies to improve low temperature emissions control
• Coordinate with BES-funded scientists to identify catalysts/technologies that have potential – Transfer “science” findings to applied settings
• Evaluate promising catalysts/technologies under exhaust-relevant conditions – H2O, CO2, CO, HC, NOx
• Investigate durability – Sulfur, aromatics, hydrothermal cycling
• Characterize catalysts/technologies to understand fundamental behavior and limitations – Particularly when performance is being impeded – Materials and specific catalyst functionality/chemistry
• Redesign catalysts trying to overcome shortcomings
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Milestones • Previous project scope was aimed at measuring the impact of advanced
combustion modes on emissions control – Low temperature reactivity seen to be a significant hurdle
• Example completed previous milestones are: – Comparison of Cu- and Fe-zeolite Urea-SCR catalyst performance for multimode diesel
engine operation – Characterization of hydrocarbon oxidation efficiency of diesel oxidation catalyst for low
load operation with advanced combustion which results in lower exhaust temperatures
• Current direction is to identify novel/innovative technologies that can be implemented to address the challenges of advanced combustion strategies
• FY13 Milestone: Characterization of performance and surface morphology for a novel candidate catalyst (September 30, 2013) – On target
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Collaborations • Basic Energy Sciences [active]
– Sheng Dai and Steve Overbury (ORNL) – Center for Nanophase Material Science (ORNL)
• Interactions with other fundamental catalysis groups [planned]
• CLEERS [active] – Dissemination of data; presentation at CLEERS workshop
• USCAR/USDRIVE [active and future activities] – Participation in US DRIVE 2012 Low Temperature Workshop
• ACEC catalyst sub-team (GM, Ford, Chrysler, PNNL, ORNL) – Guidance of critical technology needs
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Summary of Technical Accomplishments • Investigated innovative Au@Cu (core@shell) catalyst for oxidation
– Copper oxide surrounding Au core shows excellent low temperature CO oxidation behavior • In presence of CO2 and H2O
– Inhibition by HC and NOx observed • Could be potential CO-cleanup catalyst at tailpipe
– Durability investigated up to 800°C • Performance is good up to 700°C, but falls off 800°C; Sintering observed
• Demonstrated synergy of mixing of Au@Cu and Pt catalysts and potential to overcome inhibitions – Pt inhibited by CO at low temperature; improved with AuCu – Very high NO to NO2 oxidation observed with mixture
• Synthesized and evaluated new catalysts using a new support – Improved hydrothermal durability using ceria-zirconia support
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Synthesis of AuCu/SiO2 Catalyst • Supported Au nanoparticles serve as templates to synthesize small
and disperse intermetallic AuCu nanoparticles – Synthesized using aqueous/solution techniques
H. Zhu et al. Applied Catalysis A: General 2007, 326, 89-99 Bauer et al. Phys. Chem. Chem. Phys., 2011, 13, 2571-2581
Oxidized catalyst Au core + CuOx shell
SiO2
Au(en)2Cl3 pH=10
(1.0 M NaOH) SiO2
H2N
NH2
H2N
NH
Au
N N
amine ligand coats the surface of gold
Cu(C2H3O2)2
Organic solution at 300゜C
Cu0
Reduction H2 ~150 ゜C
Reduced catalyst = AuCu Alloy (Inactive)
SiO2
Metallic Cu addition
Reduce in H2 ~150 ゜C SiO2
Au Au
Au Au Au
SiO2 Au Au
Au Au Au
SiO2 Oxidation
When reduced, catalyst forms a
AuCu alloy Inactive for CO
oxidation
When oxidized, catalyst forms
Au@Cu core-shell
ACTIVE for CO oxidation
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AuCu/SiO2 catalyst is activated under lean conditions; forms core (Au) shell (CuOx) • When oxidized, Au
core surrounded by amorphous CuOx shell after heating at 500 °C
• After H2 reduction at 300 °C, AuCu alloy forms – Time required to
be reduced – Brief rich period
will not inactivate catalyst
Oxidation
Au
CuOx ACTIVE
Inactive
Au 38.2
2θ
AuCu 40.3
2θ
Reduction
Au 38.2
2θ
AuCu 40.1
2θ
AuCu alloy
Oxidation pretreatment conditions: Flow Rate = 75 sccm 550 ̊C for 16 in 10% O2 + 1% H2O in Ar
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0
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1
0 50 100 150 200 250 300 350 400 450 500 550
CO
Con
vers
ion
Temperature (°
C)
AuCu/SiO2 W/F = 0.50 g·h/mol
AuCu/SiO2 W/F = 0.25 g·h/mol
Pt/Al2O3 W/F = 0.50 g·h/mol
Pt/Al2O3 W/F = 0.25 g·h/mol
Catalyst = 50-100 mg 10% O2 1% H2O 1% CO Ar (balance) Flow Rate = 75 sccm
Au@Cu/SiO2 catalyst is excellent for low temperature CO oxidation
• Au@Cu/SiO2 shows high activity even at 50°C – Reactivity as low as 0 °C
• Similar loadings of Pt/Al2O3 catalyst show little activity below 200°C – T50% = 182-205 °C – Pt/Al2O3 space velocity: W/F = 0.5 g·h/mol is 27k h-1
CO-only oxidation
[weight catalyst (g)] W/F = ––––––––––––––––––– [molar gas flow (mol/h)]
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Low temperature activity is limited in the presence of NO and hydrocarbons • Strong inhibition by both NO and HC • Pt/Al2O3 displays less impact, but still
shows inhibition
• Opportunity exists as a low temperature CO-cleanup catalyst for Au@Cu – Passive SCR approach presented by Jim Parks in prior talk (ACE033) shows CO-only
exhaust concerns
0 50 100 150 200 250 300 350 400 450 500 550
0.0
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0.8
1.0
CO C
onve
rsio
n
Temperature (oC)
1% CO
AuCu/SiO2
1% CO + 0.1% C3H6 + 0.05% NO
1% CO + 0.1% C3H6
1% CO + 500 ppm NO
1% CO
0 50 100 150 200 250 300 350 400 450 500 550
0.0
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1.0
CO C
onve
rsio
nTemperature (oC)
1% CO + 0.1% C3H6 + 0.05% NO
1% CO + 0.1% C3H6
1% CO + 500 ppm NO
1% CO
Pt/Al2O3
Catalyst = 50 mg 10% O2 1% H2O CO, NO, C3H6 as listed Ar (balance) Flow Rate = 75 sccm
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Combination of Au@Cu/SiO2 and Pt/Al2O3 studied to explore potential synergies
• Au@Cu/SiO2 and Pt/Al2O3 were physically mixed together
• CO oxidation activity increases compared to Pt/Al2O3 – but not as high as
Au@Cu/SiO2 alone
0
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0 75 150 225 300 375 450 525
CO
Con
vers
ion
Temperature (°
C)
W/F = 0.50 g·h·mol-1
Au@Cu/SiO2
Au@Cu + Pt
Pt/Al2O3
CO-only oxidation
Catalyst = 100 mg 10% O2 1% H2O 1% CO Ar (balance) Flow Rate = 75 sccm
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NO oxidation synergy observed with Au@Cu/SiO2 + Pt/Al2O3 physical mixture • Improved low temperature CO-oxidation
in the presence of NO w/ Au@Cu+Pt – Better than either individual catalyst
• For Au@Cu+Pt, NO oxidation to NO2 approaches equilibrium limit at 250°C
• Considerably more active than Pt/Al2O3
Theory: 1. NO oxidation inhibited by CO on Pt 2. Au@Cu catalyst oxidizes CO, thus improving NO oxidation
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30 40 50 60 70 80 90
Inten
sity (
Arb.
Units
)
Degrees (2θ)
As-synthesized AuCu/SiO2
Au-CuO/SiO2 – 800 ゜C, 10h
75 150 225 300 375 450 525
0.0
0.2
0.4
0.6
0.8
1.0
CO C
onve
rsio
n
Temperature (oC)
W/F = 0.249 g·h/mol 10% O2 1% H2O 1% CO Ar (balance) Flow Rate = 75 sccm
Durability a concern with SiO2 support • Au@Cu/SiO2 aged in 10% O2 + 1% H2O in Ar
• Catalyst relatively stable up to 700°C – Only very low temperature activity (T< 150°C)
diminishes with increasing aging temperature
• Particles grow up to ~25 nm in diameter after thermally aged at 800°C for 10h (8-9 nm avg.) – Sulfur also shown to strongly deactivate
• Improved metal support interactions needed
800 ̊C, 10h
50nm
500
C, 10h CO-only
oxidation
0123456789
10
Fresh 600C10h
700C10h
800C10h
Avg
. Par
ticle
Dia
met
er (n
m)
Aging Temperature (°C)
XRD
XRD
XRD
XRD
TE
M
TEM
TEM
TEM
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0.0
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1.0
0 50 100 150 200 250 300 350 400 450 500 550
CO
Con
vers
ion
Temperature (°C)
Au@Cu/CeO2(75)-ZrO2(25)
AuCu-550C 16h600C 16h700C 16h800C 16h
W/F = 0.25 g*h/mol 10% O2 1% H2O 1% CO Ar (balance) Flow Rate = 75 sccm
Supporting AuCu catalyst on ceria-zirconia shows improved stability • Same synthesis procedure as
followed as described in slide 10
• Even with low weight loading high activity shown with unaged sample – W/F = 0.25 g*h/mol
• SV = ~95,000 h-1; denser than SiO2 – T50% = 60°C – T90% = 98°C
• Activity drops after aging at 800°C, but is still very high – T50% = 125°C – T90% = 155°C
Aging Temp.
CO-only oxidation
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Catalysts studied show promise, but challenges remain • T-90 compared for each catalyst and
condition studied – T-90 = temperature where 90%
conversion is achieved – The lower the better
• 90% Oxidation of HCs and CO at 150°C will continue to be difficult, but exploiting synergies of catalysts show promise – Both Au@Cu/SiO2 and Pt/Al2O3 show
impact from NO and HCs – Mixing catalysts results in ~35°C
drop in T-90
• Matching active catalysts with the right support shows promise for overcoming durability challenges – 90% conv. achieved w/ 800°C aging
050
100150200250300350400
CO-only CO+NO CO+NO+HC
CO-o
xidat
ion
T-90
(°C)
AuCu/SiO2Pt/Al2O3Mixture
Au@Cu/SiO2 Pt/Al2O3 Mixture
Goal
050
100150200250300350400
Fresh Aged at 800°C
CO-o
xidat
ion
T-90
(°C)
AuCu/SiO2AuCu/CZAu@Cu/SiO2 Au@Cu/Ceria-Zirconia Goal
Goal
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Future work • Continue investigation on Au@Cu with ceria-zirconia and other supports
– Activity in the presence of HC and NO – Physical mixture with Pt/Al2O3; Pt co-supported on ceria-zirconia – Additional supports while studying/characterizing metal support interactions
• Specifically interested in titania-modified SiO2 support – Discussed briefly last year and this year in CLEERS project (ACE022)
• Initial focus is on oxidation catalysts, but future efforts will move into trap materials and NOx reduction catalysts – Low temperature NOx and HC trap materials
• Release at moderate temperatures – NOx storage reduction catalysis with low temperature release and highly active
reduction chemistry
• Goal is to move from powder catalysts to washcoated cores and further validation in engine exhaust – Developing washcoating capability
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Summary • Relevance:
– Advanced combustion modes have greater efficiency and consequently lower exhaust temperatures – Simultaneous increase in efficiency and decrease in allowable emissions necessitates improved
emissions control system performance, especially at low temperatures
• Approach: – Pursue innovative catalyst technologies to improve low temperature emissions control – Evaluate performance, investigate durability, characterize materials, identify fundamental limitations
• Collaborations: – Basic Energy Science scientists, CLEERS, USCAR/USDRIVE
• Technical Accomplishments: – Investigated activity, durability and material properties of Au@Cu core-shell oxidation catalyst – Identified synergistic effects of physical mixture of Au@Cu and Pt catalysts that overcome some of
the observed inhibitions – Synthesized new catalysts with a range of supports, that significantly improve durability
• Future Work: – Continue investigation on AuCu with ceria-zirconia and other supports – Move into NOx reduction catalysts and trap materials – Move from powder catalysis to washcoated cores and further validation in engine exhaust
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Technical back-up slides
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DRIFTS analysis shows NO interactions on catalysts are unstable above 200°C
• Evidence of NO adsorbed on AuCu/SiO2
– Nitrates: 1300-1650 cm-1 – Chemisorbed on Au; faintly at
~1880 cm-1
• Heating nitrated samples while flowing NO+O2 results in removal at 200°C
– Coincides with CO-lightoff
-0.04
-0.02
0.00
0.02
0.04
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0.10
0.12
0.14
130015001700190021002300
Abs
orba
nce
Wavenumber (1/cm)
500 C
400 C
350 C
300 C
250 C
200 C
150 C
100 C
50 C
-0.01
0.00
0.01
0.02
0.03
130015001700190021002300
Abs
orba
nce
0.1% NO + 10% O2 on AuCu/SiO230 min25 min20 min15 min10 min 5 min 0 min
0 50 100 150 200 250 300 350 400 450 500 550
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CO C
onve
rsio
n
Temperature (oC)
1% CO
AuCu/SiO2
1% CO + 0.1% C3H6 + 0.05% NO
1% CO + 0.1% C3H6
1% CO + 500 ppm NO
1% CO
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1000
2000
3000
4000
5000
6000
7000
8000
9000
30 35 40 45 50 55 60 65 70 75 80 85 90
Inte
nsity
Degrees (2 Theta)
Aging Au@Cu/SiO2 as-synthesized 600 C for 10h 700 C for 10 h 800 C for 10h
Scherrer Analysis = 7.3 nm, TEM = 8.7 nm
700 ̊C, 10 h
Scherrer Analysis = 9.0 nm, TEM = 8.4 nm
Scherrer Analysis = 5.7 nm, TEM = 5.9 nm
Scherrer Analysis = 4.0 nm
600 ̊C, 10 h
as-synthesized
800 ̊C, 10 h
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This sample is different from the two above. This sample was from the first Au@Cu batch that was heated 500, 600, 700 and 800 C.
Heated at 600 C for 10 h.
Heated at 700 C for 10 h.
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600 C, 10h 700 C, 10h
800 C, 10h 800 C, 10h
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0%
10%
20%
30%
40%
50%
60%
70%
80%
90%
100%
0 50 100 150 200 250 300 350 400 450 500 550
CO C
onve
rsio
n
Temperature (°C)
Au/CeO2(0.75)-ZrO2(0.25)
550C, 16h600C, 16h700C, 16h800C, 16h
Flow rate = 75 sccm W/F = 0.25 g*h/mol SV = ~95,000 h-1 1% CO + 1% H2O + 10% O2 + Ar
Aging Temp.
Au-only catalyst supported on ceria-zirconia also shows good stability • Even with low weight loading high
activity shown with unaged sample – W/F = 0.25 g*h/mol
• SV = ~95,000 h-1
– T50% = 50°C – T90% = 94°C
• Activity drops after aging at 800°C, but is still very high – T50% = 103°C – T90% = 182°C