Numerical study of the thermohydraulic performance of printed circuit … · 2019. 3. 12. · Why...
Transcript of Numerical study of the thermohydraulic performance of printed circuit … · 2019. 3. 12. · Why...
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2nd International Conference on Sustainable Energy
and Resource Use in Food Chains
RCUK Centre for Sustainable Energy Use in Food Chains
Numerical study of the thermohydraulic
performance of printed circuit heat
exchangers for supercritical CO2 Brayton
cycle applications
Lei Chai*, Savvas A Tassou
Institute of Energy Futures, Brunel University London
Paphos, Cyprus 17-19 October 2018
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Outline• Introduction
– Why sCO2? Why printed circuit heat exchanger?
• Computational method
– Element, model, boundary condition.
• Data acquisition
– Local, average and overall parameters.
• Results and discussion
– Thermohydraulic performance, comparison with correlations.
• Future work
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Why sCO2?
• working fluid with a
high power density
• smaller equipment sizes
• smaller plant footprint
• lower capital cost
• use of standard materials
• improved electrical-power-
conversion efficiency
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Why printed circuit heat exchanger?
Recuperator
• increase the average
temperature of the heat source
• results in higher efficiencies
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Why printed circuit heat exchanger?
• highly compact construction
• high heat transfer coefficient
• high pressure capability
• wide range of operating
temperatures
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Computational element and model
• standard k-ε model
• NIST real gas
thermophysical
properties
• buoyant effect
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Boundary and operating conditions
• Periodic for upper and lower surfaces
• Symmetry for left and right surfaces
• Mass-flow-rate for two inlet
• Pressure-outlet for two outlet
• Mass flux balances: 254.6 to 1273.2 kg/(m2·s)
• Cold side :100 °C of inlet temperature and 150 bar of outlet pressure
• Hot side: 400 °C of inlet temperature and 75 bar of outlet pressure
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Data acquisition
Local thermohydraulic parameters
Average thermohydraulic parameters
Overall thermohydraulic parameters
z
z
GDRe
z
z
w,z f,z
qh
T T
z
z
f,z
h DNu
2z
z f2 D dp
Gf
dz
z0
L
Re dzRe
L z0
L
h dzh
L z0
L
Nu dzNu
L z0
L
f dzf
L
m
UQ
A T
hi co ho ci
m
hi co
ho ci
( ) ( )
ln( )
T T T TT
T T
T T
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Validation of CFD model
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Local heat transfer coefficient
G = 763.9 kg/(m2·s)
z = 136 mm
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Local pressure drop
G = 763.9 kg/(m2·s)
z = 136 mm
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Average thermohydraulic performance
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Overall thermohydraulic performance
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Comparison with prediction from empirical correlation
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Comparison with prediction from empirical correlation
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Future work – modeling for heater, recuperator, cooler
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Future work - numerical study for different flow passages
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Future work – sCO2 heat exchanger test facility
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Acknowledgements
• Engineering and Physical Sciences Research Council (EPSRC) of the UK
under research grants EP/P004636/1 and EP/K011820/1
• European Union’s Horizon 2020 research and innovation programme
under grant agreement No. 680599.
• The authors would like to acknowledge the financial support received by
the project funders and the industry partners.
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Thank you !
Lei Chai Savvas A Tassou