NAME              = three_layers_LiBi
----------------------------------------------------------------------
# Geometry ---> blockMeshDict, setField, probes, singleGraph  (in mm)
h_P = 10 
h_E = 10
h_N = 40
L_x = 80 
----------------------------------------------------------------------
# Mesh ---> blockMeshDict
N_PE = 256 
N_E  = 128
N_NE = 256
N_X  = 1600
----------------------------------------------------------------------
# cyclic mesh: 1, wall mesh: 0
cyclicMesh = 0
allPre     = allPre
collated   = true
----------------------------------------------------------------------
# Simulation ---> contolDict
End_Time		= 900
initialTimeStep = 0.001
maxDeltaT       = 0.002
MaxCoNumber     = 0.5
writeInterval	= 0.1
----------------------------------------------------------------------
# Parallel ---> decomposeParDict
N_Processor	= 16
------------------------------------------------------------------
# globalProperties ---> globalProperties
referenceMassConcentration = 7.062e+01
initialMassConcentration = 7.062e+01
referenceTemperature = 450
currentDensity       = 0.01e4
------------------------------------------------------------------
# functions to include
probingFunc = 1
----------------------------------------------------------------------
# Parameter ---> transportProperties; set to 0 to switch off thermal conv.
betaT		= 1
----------------------------------------------------------------------
# switch mass transport in P ---> constant/regionProperties (on = 1, off = 0)
massTransportSwitch = 1
----------------------------------------------------------------------
# Numerical Solution Algoritm PIMPLE ---> fvSolution
nCorrectors	 = 20
nOuterCorrectors = 3
fCorrectors      = 250
----------------------------------------------------------------------
# fvSchemes --> ddt (backward, Euler, ...)
ddtSchemes = Euler
----------------------------------------------------------------------
# Solid-Fluid ---> constant/regionProperties (solid = 0, fluid = 1)
negativeElectrode   = 1
electrolyte         = 1
positiveElectrode   = 1
----------------------------------------------------------------------
# Boundary conditions --> allPre (noSlip,continousVelocity)
PressureAtInterface     = fixedFluxPressure
VelocityAtInterface     = continuousVelocity
----------------------------------------------------------------------
# Boundary conditions --> 0.orig
Temperature_TOP     = 450
Temperature_BOT     = 450
initialUniformTemperature  = 450
initialTemperatureProfile  = false #pure conduction profile as start condition
----------------------------------------------------------------------
# Electrode materials
Li(in Bi) | KCl_LiCl | Li
----------------------------------------------------------------------
# Material properties of positive electrode at T = 450
density_P = 8.576e+03
heatCapacity_P = 1.7e+02
thermalConductivity_P = 1.421e+01
electricalResistivity_P = 1.39e-06
viscosity_P = 1.304e-07
thermalExpansion_P = 1.362e-04
internalHeat_P = 0.000e+00
valencyNumber_A = 1
# relevant for mass transport:
molarMass_A = 6.940e-03
massExpansion_AB = 2.122e-3
massTransportDiffusivity_AB = 7.0e-09
----------------------------------------------------------------------
# Material properties of Electrolyte at T = 450
density_E = 1.648e+03
heatCapacity_E = 1.330e+03
thermalConductivity_E = 6.904e-01
electricalResistivity_E = 6.358e-03
viscosity_E = 1.983e-06
thermalExpansion_E = 3.2e-04
internalHeat_E = 0.000e+00
----------------------------------------------------------------------
# Material properties of negative electrode at T = 450
density_N = 4.911e+02
heatCapacity_N = 4.237e+03
thermalConductivity_N = 5.218e+01
electricalResistivity_N = 3.27e-07
molarMass_N = 6.940e+00
valencyNumber_N = 1
viscosity_N = 7.13e-07
thermalExpansion_N = 1.923e-04
internalHeat_N = 0.000e+00
----------------------------------------------------------------------
