gpf model-based optimization methodologies supporting rde
TRANSCRIPT
GPF model-based optimization methodologiessupporting RDE conformity
Michail Mitsouridis, Aristotle University ThessalonikiGrigoris Koltsakis, Aristotle University ThessalonikiZissis Samaras, Aristotle University ThessalonikiStefan-Herbert Veit, AVL List GmbHChristian Martin, AVL List GmbH
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• The results presented here were obtained within the project UPGRADE.This project has received funding from the European Union’s Horizon 2020 research and innovation programme under grant agreement No 724036.
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Acknowledgements
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UPGRADE project structure
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Motivation
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Ultra-clean gasoline engines via (c)GPF & Exhaust After Treatment (EAT) system optimization
In this respect:– 13 (c)GPFs of different cell- and wall micro-structure were tested
– Based on the test results, predictive deltaP and filtration models were developed
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ModelInputs / outputs
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INPUTS
Mass flow rate
Temperature
Soot emissions
DESIGN & CONTROL PARAMETERS
Sizing
Catalyst technology
Substrate technology
Positioning
Engine fueling strategies
…
OUTPUTS
Filtration efficiency
deltaP
MODEL
Flow modeling
Filtration modeling
Kinetic modeling
Heat transfer modeling
deltaP model
• Soot-free wall permeability
• Soot loaded wall permeability
• Soot cake permeability
Filtration model
• Diffusion coefficient
• Interception coefficient
• Gradient coefficient
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ModelTunable parameters
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Predictive flow resistance toolas a function of wall micro-structure
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1 8 3
6
B
A A
1
8 3
6 B
GPF A (UF: 100g/l) and B (CC: 50g/l)deltaP and filtration performance investigation
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deltaP & filtration efficiency prediction forcGPF A and cGPF B
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• Experimental & simulation deltaP and filtration efficiency results.• SYSTEM B has better deltaP and worse filtration performance compared to SYSTEM A due to its higher
effective porosity.
UF: 100 g/l CC: 50 g/l
(100g/l w/c loading) (50g/l w/c loading)
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Model validationby driving cycle tests
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The original exhaust system was removed and replaced with exhaust
systems of two different variants:
(100g/l w/c loading)
UF: 100 g/l
CC: 50 g/l
(50g/l w/c loading)
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deltaP model validationRDE aggressive test cycles
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Soot lo
aded
initia
l sta
te
0.1 g/l 0.4 g/l
UF: 100 g/l CC: 50 g/l
Soot-
free
initia
l sta
te
The model is able to accurately predict deltaP for filters at both soot-free and soot loaded conditions
0 g/l 0 g/l
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Effect of soot loading on filtration performanceRDE moderate test cycle
• ~500°C appears to be the threshold above which soot oxidation takes place• The model is able to predict the significant effect of soot accumulation on a
GPF’s filtration performance
FE: 98% FE: 98%
FE: 86%FE: 87%
UF: 100 g/l CC: 50 g/l
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Effect of cGPF placement on filtration performanceRDE aggressive test cycle
CC 50 g/l GPF regenerates faster due to higher temperature➔ soot mass drops below 100% FE threshold level
UF: 100 g/l CC: 50 g/l
FE: 86%
0.16
FE<99.5%
FE<99.5%
0.02 g/l 0.16 g/l
FE: Filtration Efficiency
0.02
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Validation of model explanation with FCOff deactivationRDE aggressive test cycle
withfuel cut-off events
withoutfuel cut-off events
FE: 86%
FE: 98%
To validate that the CC filter deteriorated filtration performance is associated to its enhanced passive regeneration capability, the test was repeated de-activating fuel cut-off events to limit passive regeneration
By deactivation of fuel-cut off mode the GPF retains its high filtration efficiency
CC: 50 g/l
FCOff: Fuel Cut-Off
• Soot loading has an important beneficial effect to maintain RDE compliance w.r.t. filtration efficiency.
➔Careful management of the regeneration events desirable to avoid complete regenerations
• Multitude of exhaust line design parameters, such as:
– filter positioning (affecting temperature levels)
– washcoat amount (affecting filtration performance)
– engine fueling strategies
create a very demanding optimization problem.
➔ Employment of model-based methodologies can reduce development efforts and associated costs
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Conclusions
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Thank you very much!
17/5/2019 15SIA Powertrain, Rouen 2014
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