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Modeling & Simulation of Solid Oxide Fuel Cell Using COMSOL MULTIPHYSICS ®
Yi-Xiang SHI(史翊翔)Supervisor : Prof. Ning-Sheng CAI(蔡宁生)Department of Thermal EngineeringTsinghua University,Beijing, China
2006-12
Presented at the COMSOL Users Conferences 2006 Shanghai & Beijing
Why Solid Oxide Fuel Cell?
Extremely high efficiency ( Generation alone: 50-60%
SOFC/GT hybrid:60-75%Cogeneration : 80-90%)
High fuel flexibility (Hydrogen, coal syngas, biogas,various
hydrocarbon fuels, et al)
Low emissions without additional cleanupunit & secondary pollutants (near-zero SOx
,NOx, particle, be promising in CO2 capture )
Appropriate in both central & distributed power plant
From http://www.siemens.com
Why Modeling and Simulation?
• To understand the complex coupling transport and reaction processes
• To do parameter studies after comprehensive validation• Porous electrode microstructure• Operating conditions (Temperature, Pressure,Gas composition,…)
• To substitute some expensive, time-consuming, labor-intensive experiments• Detailed mechanistic model may lead to significant design
improvement
• To provide the fundamentals of SOFC-based hybrid system R&D
Mechanistic modeling methodology
Deb
ug&
Sen
sitiv
ity a
naly
sis
Mul
tidim
ensi
onal
th
eore
tical
moe
del
Anode-Supported SOFC button cell modeling
O2-
e-
H2 H2O
O2
O2-
e-
TPB
Anode active interlayer
Electrolyte layer
Cathode layer
Anode support layer
electronic conductor electronic conductor
Contact angle
ionic conductorionic conductor
Three phase boundary
• Button cells are widely used in SOFC experimental studies for its simple experiment setup and operation
• For detailed mechanistic model validation, button cell test data:• Easier to achieve, have better reliability& repeatability
Photograph and SEM micrograph of button cell
Assumptions:Steady state conditions; Iso-thermal; Ideal gasUniform active surface area Pressure driven flow neglectedTwo conducting phases: continuous and homogeneous
an-spΩ
elecΩcaΩca/ac∂Ω
ca/elec∂Ω
elec/an_act∂Ω
an-sp/fc∂Ω
symmetry∂Ωelec/ac∂Ω
an-actΩ
an-act/an-sp∂Ω
Calculation domain--Simplified to 2-D for
axis symmetry
Modeling Methodology
Ionic/electronicCharge balance
(Ohm’s law,B-V equation)
Open circuit voltage(Nernst equation, leak overpotential)
Mass balance(Dusty-gas model)
Operatingconditions
Cell VoltageCell Voltage
Parameters distributions;Polarization curves
Parameters distributions;Polarization curves
Electrochemical Reactions Kinetics
MechanisticMechanisticmodelmodel
Meshing in COMSOL MULTIPHISICS®
Conversional T-mesh
Structured Quad Mesh Generation Mesh Density Control Based on Mapping Approach X = (1+tanh(a*theta))/2
Model validation in the base case
H2 and H2O concentration distribution at anode in the base case
Un-uniformity at the anode due to the electrochemical reactions and asymmetric button-cell electrode
Reaction zone distribution
AnodeCathode
Modeling results by changing tortuosity
The model could not predict the experimental data well until the tortuosity was adjusted to 14
Model Calibration in the base case
Experimental tortuosity :Usually 2~10For conventional SOFC thick anode :2~5 (Williford et al,2003)
(Anil V. Virkar, 2003 )(Anil V. Virkar, 2003 )
•Totuosity in the model have to be tuned to 17
Modifications to hydrogen concentration at the TPB
electronic conducterelectronic conducter
ionic conducterionic conducter
Ni YSZTPB
Inter Inter
H2O,CO2
Surface Diffusion
AdsorptionAdsorption
Fuel(H2,CO,etc)Products(H2O,CO2,etc)
O2-
TPB
H2,CO,etc
Surface
Diff
usion
TPBiC
TPB,ViC
• Figure out the source of large diffusion resistance near the TPB at high fuel utilization or large current density
2 1
Molecular diffusionKnudsen diffusion, etc
Competitive adsorptionSurface diffusion
Electric analogue circuit of H2 diffusion
Model Validation
Operating Conditions: 800℃ 101,325 pa; Oxidant:0.21 O2, 0.79 N2
0 20000 40000 60000 80000
0.2
0.4
0.6
0.8
1.0
H2,experimental85% H2+15% H2O,experimental50% H2+50% H2O,experimental35% H2+65% H2O,experimental20% H2+80% H2O,experimental Baseline for parameter estimation Calculated
Volta
ge/V
Current Density/(A/m2)
Model agreed well with published experimental data without any other calibrations after the parameter estimation according to the baseline (Anil V. Virkar, 2003 )
Some of the modeling results
0.0 0.1 0.2 0.3 0.4 1.2 1.3 1.4
0
4000
8000
12000
16000
Ionic,85% H2,15% H2O Electronic, fuel:85% H2,15% H2O Ionic,fuel:20% H2,80% H2O Electronic,fuel:20% H2,80% H2O
Cur
rent
den
sity
/(Am
-2)
x/mm
elec elec j( )eV J Qσ−∇⋅ ∇ − =r ( )i i ij u Rρω∇ ⋅ + =
rr r
( )k p Fρη
∇⋅ − ∇ =r
T( ( ) ) ( )u u u u p Fη ρ−∇⋅ ∇ + ∇ + ⋅∇ +∇ =rr r r r
p( )k T C Tu Qρ∇⋅ − ∇ + =r
Generalized Unit Cell Mechanistic Model
Coupling
Model Geometry
Air channel
Fuel channel
Anode
Cathode
Electrolyte
Interconnect
Interconnect
Tubular SOFC - Axial Tubular SOFC- Cross
Model Validation
1002003004005006000.4
0.5
0.6
0.7
0.8 Axial direction modeling results Experimental data(Siemens-Westinghouse)
Cel
l V
olta
ge/V
Current Density / (mA/cm2)Model validation in axial direction Model validation in cross direction
1002003004005006000.4
0.5
0.6
0.7
0.8 Cross direction modeling results Experimental data(Siemense-Westinghouse)
Cel
l Vol
tage
/V
Current density/(mA/cm2)
Operation Conditions: 1000℃ 101,325 pa; Fuel:97% H2, 3% H2O Oxidant:0.21 O2, 0.79 N2
Experimental data from:J.H. Hirschenhofer, D.B. Stauffer, R.R. Engleman, et al. Fuel Cell Hand Book (Seventh Edition), West Virginia: EG&G Technical Services, Inc. 2004. 7-31~7-44
Some of the Modeling Results
“Hot spot”area
3D planar SOFC modelingParametersAnode thickness 800um
Cathode thickness 60um
Electrolyte thickness 10um
Interconnect thickness 4 mm
Interconnect width 4 mm
Channel height 4 mm
Meshing
Extrude
EIS simulation using SOFC mechanistic transient model
Polarization is only a gross behavior of all the microcosmic processesEIS (Electrochemical Impedance Spectroscopy) is a kind of transient characterization technology, contain much more information about reaction and transport mechanism than polarization curves.
Most of the EIS are interpreted in Equivalent circuit analog
Physical& Chemicalprocesses
Physical& Chemicalprocesses
Equivalent Circuit Analog
Equivalent Circuit Analog
EIS plotEIS plot
Mechanistic model based on conservation equationsMechanistic model based on conservation equations
Much more uncertainties (form of equivalent circuit analog)
Basic ideas
Small sinusoidal perturbation in potential
Resultant current response
Magnitude Z0Phase shift φ
Real and Imaginary Component
Nyquist plotBode plot
SOFC transient Model
SOFC transient Model
Phase Shift(φ)
Normalized harmonic voltage signal imposed on button cell
Normalized observed current density signal Computer simulation is
almost the same with true experimental tests
Computer simulation is almost the same with true experimental tests
Summary
• Computer simulation in the SOFC R&D could provide insights for:• The detailed transport and reaction processes
• Improving cell design and electrode microstructure
• Commercial FEA software- Comsol Multiphysicscould be used for:• Single button cell modeling
• 2D or 3D Unit Cell modeling
• EIS modeling
Thank you ! Thank you !