Non-Destructive X-ray Measurement of Soot, Ash, Washcoat and
Transcript of Non-Destructive X-ray Measurement of Soot, Ash, Washcoat and
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Non-Destructive X-ray Measurement of Soot, Ash, Washcoat and
Regeneration Damage for DPFs
Charles E.A. Finney, Todd J. Toops, C. Stuart DawOak Ridge National Laboratory
Jan Zandhuis3DX-RAY
Thomas FoxX-Metrix
DEER
August 7, 2008
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Need for non-destructive technique for ash and soot analysis
•
Typical techniques to determine the soot and ash location require destruction of DPF–
May disrupt layers
–
Sequential measurements not possible–
Resolution along the length not possible
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Typical EPMA preparation illustrates potential ash/soot layer disruption•
First step:–
Cut into pieces–
Possible mechanical disruption
•
Second step:–
Fill channels with epoxy–
Possible disturbance of ash from the walls; flowing
•
Third step:–
Electron microprobe–
Low probability of disruption
Middle ExitInlet
Inlet Middle Exit
+ =
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Opportunity to use X-ray instrument at ORNL for short-term DPF analysis
•
Loaned from 3D X-ray (Ltd.) for 6 weeks–
MDXi
400
•
Linear low noise detector•
12 bit, 4096 gray scale levels•
Control over sample height•
Control over sample angle•
Batch file capability
–
Evolved from airport security screening devices
–
Scan can be recorded in 15s
•
Can it be used to detect ash and soot distributions in a DPF?
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Basics of X-ray imaging
Collimated line-scan imaging
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Goals of analysis
•
Measure and corroborate ash distributions from rapid ash loading projects
•
Measure soot distribution –
In-can soot distribution from engine
–
Quantification and calibration with simulated soot loading
•
Measure thermal damage in DPFs–
Purposefully damaged
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Ash Loading and Distribution
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DPF
DOC
Experimental setup for accelerated ash loading at ORNL
(ash part 1)•
517cc Hatz
Engine
is operated at 1500 RPM continuously
•
5% lube oil mixed with ULSD fuel
•
700cc DPF
•
Active regeneration
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Ash deposits observed in rear section
•
Shows good correlation to EPMA results
Flow
~7% signal
X-Ray transmission image
X-Ray transmission profile
Channels start filling Saturation all channels are filled
Inlet 150 mm
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Accelerated ash loading at MIT (ash part 2)•
Sloan Automotive Laboratory accelerated ash loading system (Sappok
et al.
–
DEER 2008)
•
DPF received in two halves–
One with ash loaded, one unusedSystem Specifications
• Exhaust heat exchangers – counter flow • Centrifugal blower – backpressure control• D5.66” x 6” DPF
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Ash in segmented DPF
•
X-ray confirms ash plugs ~4
cm from end
CLEAN FLATTENEDClean
Ash loaded
Transmission Difference
X-ray Transmission Comparison
Shifted profile
ASH FILLED FLATTENEDAsh loaded
FLOW
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Quantification of ash loading determine ash density and specific loading profile•
Area under curve correlates to ash mass
•
Local packing densities can be calculated
0.169 0.181
0.338
0.260
0.00
0.05
0.10
0.15
0.20
0.25
0.30
0.35
Field 200CPSI
Field ACT Field ACT Lab 200CPSI
Ash
Pac
king
Den
sity
[g/c
m3 ]
0 20 40 60 80 100 120
Length (mm)
0
0.05
0.1
0.15
0.2
0.25
0.3
Ash density (g/cm
3)
Observed ash plug fromdestructive analysis
•
X-ray corroborates destructive analysis–
density measurement –
approximate plug length
•
Unusual packing distribution not detected during destructive analysis–
Difficult to do through lab measurements
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Soot Loading Studies
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Controlled soot loading for calibration and quantification (part 1: laboratory soot loading)
•
75mm (0.6L) uncatalyzed Cordierite
•
Artificially vacuum loaded•
One half sooted (0.3L), other half clean (masked off)
Added Weight Loading
0
reference
0.00 g/L
1
0.59g
1.97g/L
2
1.16g
3.87g/L
3
1.77g
5.90g/L
A
B
clean
sooted
FLOW
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Lab-loaded DPF shows gradual decrease in X-ray transmission with increasing soot
DISTANCE
REFERENCE & SOOTED TRANSMISSION DIFFERENCE PROFILES
TRA
NSM
ISSI
ON
DIF
FER
ENC
E %
0.00 g
0.00 g/L
0.59 g
1.97 g/L
1.16 g
3.87 g/L
1.77 g
5.90 g/L
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X-ray response shows good correlation to soot mass in lab-loaded DPF
•
Linear regression shows good correlation to soot mass
•
Suggests detection limits of ~0.1 g
X-ray measurement of soot mass by accumulating difference signal across sooted
section
y = 2.74x + 0.03R2 = 1.00
0
0.5
1
1.5
2
0 0.2 0.4 0.6 0.8X-ray response (a.u.)
Soot
Loa
ding
(g)
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Soot loading conditions (part 2 in-can)
•
DPF was filled using exhaust from Mercedes 1.7 L engine for 5 hours –
2300 rpm, 4.2 bar condition with 2007 ULSD
•
Cordierite DPF –
14 cm x 15 cm–
5.6 liters
•
16 grams of soot loaded (2.9 g/L)
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Flow
X-Ray transmission image
Mass Difference 16.7g ( 3 g/L) soot
17.3g ( 3.1g/L) acclimatised
Flow
X-Ray transmission image
Mass Difference 16.7g ( 3 g/L) soot
17.3g ( 3.1g/L) acclimatised
Soot measurement in can
•
X-ray device can detect soot distribution at loadings of 3 g/L–
Adsorption of 0.1 g/L H2
O is detectable
•
Marginally higher soot accumulated in front section
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Soot and ash response summary
•
X-rays much more sensitive to ash than soot
•
Ease of measurement may limit absolute resolution–
However, small changes still detectable in can
Transmission Signal
Ash 30-40% 4-7%
Soot 30-40% ~1%
Soot in can ~5% ~0.1%
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Substrate Damage
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Thermal damage inside can
Flow
Simulated melt inside canned DPFSimulated melt inside canned DPF
300mm
340mm
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Conclusions•
Ash deposits are readily detectable and can be quantified
•
Corroborates other analysis techniques with increased detail and without sample destruction
•
DPF soot distribution can be measured inside and outside the can
•
Soot mass distributions can be measured
•
Possible approach that we weren’t able to perform:–
Sequential ash and soot loading to determine the distribution of soot as a function of ash accumulation
–
Direct calibration of soot/ash density and transmission attenuation
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Supplemental slides
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Dr Thomas J. FoxDr Thomas J. FoxPresidentPresidentXX--Metrix IncMetrix Inc(US Distributor for 3DX(US Distributor for 3DX--Ray Ltd)Ray Ltd)2513 Early Court2513 Early CourtVirginia Beach, VA 23454Virginia Beach, VA 23454Tel: 757Tel: 757--450450--59785978Email:Email:
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