Failing non-equil tests after merging !1496
After merging !1496 (merged) test_1p2c_nonequilibrium_tpfa test_mpnc_kinetic_box fail now on buildbot.
In the case of test_1p2c_nonequilibrium_tpfa an fv geometry cache is accessed which is not in the stencil.
Test command: /data/src/dumux/bin/testing/runtest.py "--script" "fuzzy" "--files" "/data/src/dumux/test/references/test_1p2c_nonequilibrium_tpfa-reference.vtu" "/data/build/dumux/test/porousmediumflow/1pnc/implicit/nonequilibrium/test_1p2c_nonequilibrium_tpfa-00044.vtu" "--command" "/data/build/dumux/test/porousmediumflow/1pnc/implicit/nonequilibrium/test_1p2c_nonequilibrium_tpfa params.input -Problem.Name test_1p2c_nonequilibrium_tpfa" "--zeroThreshold" "{"velocity_liq (m/s)_1":1e-15}"
Test timeout computed to be: 300
You idiot! You signed the order to destroy Earth!
- Douglas Adams, HGttG
Reading parameters from file params.input.
The H2O-N2 fluid system was configured with the following policy:
- use H2O density as liquid mixture density: true
- use ideal gas density: true
- use N2 viscosity as gas mixture viscosity: true
- use N2 heat conductivity as gas mixture heat conductivity: true
- use ideal gas heat capacities: true
-------------------------------------------------------------------------
Initializing tables for the H2O fluid properties (20000 entries).
Temperature -> min: 2.731e+02, max: 6.231e+02, n: 100
Pressure -> min: 0.000e+00, max: 2.000e+07, n: 200
-------------------------------------------------------------------------
problem uses mole fractions
Writing output for problem "test_1p2c_nonequilibrium_tpfa". Took 8.889e-01 seconds.
Assemble: r(x^k) = dS/dt + div F - q; M = grad rtest_1p2c_nonequilibrium_tpfa: /data/src/dumux/dumux/discretization/cellcentered/tpfa/fvelementgeometry.hh:536: const LocalIndexType Dumux::CCTpfaFVElementGeometry::findLocalIndex(Dumux::CCTpfaFVElementGeometry::GridIndexType, const std::vector::GridIndex>&) const [with GG = Dumux::CCTpfaFVGridGeometry > >, false, Dumux::CCTpfaDefaultGridGeometryTraits > >, Dumux::DefaultMapperTraits > >, Dune::MultipleCodimMultipleGeomTypeMapper > >, Dune::Impl::MCMGFailLayout>, Dune::MultipleCodimMultipleGeomTypeMapper > >, Dune::Impl::MCMGFailLayout> > > >; Dumux::CCTpfaFVElementGeometry::LocalIndexType = unsigned int; Dumux::CCTpfaFVElementGeometry::GridIndexType = unsigned int; typename Dumux::IndexTraits::GridIndex = unsigned int]: Assertion `it != indices.end() && "Could not find the scv/scvf! Make sure to properly bind this class!"' failed.
[behandla:19637] *** Process received signal ***
[behandla:19637] Signal: Aborted (6)
[behandla:19637] Signal code: (-6)
[behandla:19637] [ 0] /lib/x86_64-linux-gnu/libpthread.so.0(+0x12890)[0x7f3fc9448890]
[behandla:19637] [ 1] /lib/x86_64-linux-gnu/libc.so.6(gsignal+0xc7)[0x7f3fc9083e97]
[behandla:19637] [ 2] /lib/x86_64-linux-gnu/libc.so.6(abort+0x141)[0x7f3fc9085801]
[behandla:19637] [ 3] /lib/x86_64-linux-gnu/libc.so.6(+0x3039a)[0x7f3fc907539a]
[behandla:19637] [ 4] /lib/x86_64-linux-gnu/libc.so.6(+0x30412)[0x7f3fc9075412]
[behandla:19637] [ 5] /data/build/dumux/test/porousmediumflow/1pnc/implicit/nonequilibrium/test_1p2c_nonequilibrium_tpfa(+0xd0faf)[0x55c4b4287faf]
[behandla:19637] [ 6] /data/build/dumux/test/porousmediumflow/1pnc/implicit/nonequilibrium/test_1p2c_nonequilibrium_tpfa(_ZNK5Dumux41NonEquilibriumLocalResidualImplementationINS_10Properties4TTag35OnePTwoCThermalNonequilibriumCCTpfaELb0EE11computeFluxERKNS_36OnePTwoCThermalNonequilibriumProblemIS3_EERKN4Dune6EntityILi0ELi2EKNS9_8YaspGridILi2ENS9_22EquidistantCoordinatesIdLi2EEEEENS9_10YaspEntityEEERKNS_23CCTpfaFVElementGeometryINS_20CCTpfaFVGridGeometryINS9_8GridViewINS9_25DefaultLeafGridViewTraitsISF_EEEELb0ENS_31CCTpfaDefaultGridGeometryTraitsISP_NS_19DefaultMapperTraitsISP_NS9_35MultipleCodimMultipleGeomTypeMapperISP_NS9_4Impl14MCMGFailLayoutEEESV_EEEEEELb0EEERKNS_28CCTpfaElementVolumeVariablesINS_21CCGridVolumeVariablesINS_38CCTpfaDefaultGridVolumeVariablesTraitsIS6_NS_43NonEquilibriumVolumeVariablesImplementationINS_27OnePNCVolumeVariablesTraitsINS9_11FieldVectorIdLi4EEENS_12FluidSystems11OnePAdapterINS19_5H2ON2IdNS19_18H2ON2DefaultPolicyILb1EEEEELi0EEENS_24NonEquilibriumFluidStateIdS1F_EENS_12SolidSystems15InertSolidPhaseIdNS_10Components8ConstantILi1EdEEEENS_15InertSolidStateIdS1N_EEdNS_25NonEquilibriumModelTraitsINS_30OnePNCUnconstrainedModelTraitsINS_17OnePNCModelTraitsILi2ELb1ELi2EEEEELb0ELb1ELi1ELi1ELNS_18NusseltFormulationE1ELNS_19SherwoodFormulationE0EEEEENS_21OnePNCVolumeVariablesIS1Y_EELb0ELb1ELi1EEEEELb0EEELb0EEERKNS_26CCTpfaSubControlVolumeFaceISP_NS_31CCTpfaDefaultScvfGeometryTraitsISP_EEEERKNS_31CCTpfaElementFluxVariablesCacheINS_28CCTpfaGridFluxVariablesCacheIS6_NS_44PorousMediumFluxVariablesCacheImplementationIS3_LNS_20DiscretizationMethodE2EEENS_50PorousMediumFluxVariablesCacheFillerImplementationIS3_LS2G_2EEELb0ENS_26CCTpfaDefaultGridFVCTraitsIS6_S2H_S2J_EEEELb0EEE+0x1713)[0x55c4b431b873]
[behandla:19637] [ 7] /data/build/dumux/test/porousmediumflow/1pnc/implicit/nonequilibrium/test_1p2c_nonequilibrium_tpfa(_ZNK5Dumux15CCLocalResidualINS_10Properties4TTag35OnePTwoCThermalNonequilibriumCCTpfaEE8evalFluxERKNS_36OnePTwoCThermalNonequilibriumProblemIS3_EERKN4Dune6EntityILi0ELi2EKNS9_8YaspGridILi2ENS9_22EquidistantCoordinatesIdLi2EEEEENS9_10YaspEntityEEERKNS_23CCTpfaFVElementGeometryINS_20CCTpfaFVGridGeometryINS9_8GridViewINS9_25DefaultLeafGridViewTraitsISF_EEEELb0ENS_31CCTpfaDefaultGridGeometryTraitsISP_NS_19DefaultMapperTraitsISP_NS9_35MultipleCodimMultipleGeomTypeMapperISP_NS9_4Impl14MCMGFailLayoutEEESV_EEEEEELb0EEERKNS_28CCTpfaElementVolumeVariablesINS_21CCGridVolumeVariablesINS_38CCTpfaDefaultGridVolumeVariablesTraitsIS6_NS_43NonEquilibriumVolumeVariablesImplementationINS_27OnePNCVolumeVariablesTraitsINS9_11FieldVectorIdLi4EEENS_12FluidSystems11OnePAdapterINS19_5H2ON2IdNS19_18H2ON2DefaultPolicyILb1EEEEELi0EEENS_24NonEquilibriumFluidStateIdS1F_EENS_12SolidSystems15InertSolidPhaseIdNS_10Components8ConstantILi1EdEEEENS_15InertSolidStateIdS1N_EEdNS_25NonEquilibriumModelTraitsINS_30OnePNCUnconstrainedModelTraitsINS_17OnePNCModelTraitsILi2ELb1ELi2EEEEELb0ELb1ELi1ELi1ELNS_18NusseltFormulationE1ELNS_19SherwoodFormulationE0EEEEENS_21OnePNCVolumeVariablesIS1Y_EELb0ELb1ELi1EEEEELb0EEELb0EEERKNS_31CCTpfaElementFluxVariablesCacheINS_28CCTpfaGridFluxVariablesCacheIS6_NS_44PorousMediumFluxVariablesCacheImplementationIS3_LNS_20DiscretizationMethodE2EEENS_50PorousMediumFluxVariablesCacheFillerImplementationIS3_LS2A_2EEELb0ENS_26CCTpfaDefaultGridFVCTraitsIS6_S2B_S2D_EEEELb0EEERKNS_26CCTpfaSubControlVolumeFaceISP_NS_31CCTpfaDefaultScvfGeometryTraitsISP_EEEE+0x2e3)[0x55c4b431bf03]
[behandla:19637] [ 8] /data/build/dumux/test/porousmediumflow/1pnc/implicit/nonequilibrium/test_1p2c_nonequilibrium_tpfa(_ZNK5Dumux15FVLocalResidualINS_10Properties4TTag35OnePTwoCThermalNonequilibriumCCTpfaEE17evalFluxAndSourceERKN4Dune6EntityILi0ELi2EKNS5_8YaspGridILi2ENS5_22EquidistantCoordinatesIdLi2EEEEENS5_10YaspEntityEEERKNS_23CCTpfaFVElementGeometryINS_20CCTpfaFVGridGeometryINS5_8GridViewINS5_25DefaultLeafGridViewTraitsISB_EEEELb0ENS_31CCTpfaDefaultGridGeometryTraitsISL_NS_19DefaultMapperTraitsISL_NS5_35MultipleCodimMultipleGeomTypeMapperISL_NS5_4Impl14MCMGFailLayoutEEESR_EEEEEELb0EEERKNS_28CCTpfaElementVolumeVariablesINS_21CCGridVolumeVariablesINS_38CCTpfaDefaultGridVolumeVariablesTraitsINS_36OnePTwoCThermalNonequilibriumProblemIS3_EENS_43NonEquilibriumVolumeVariablesImplementationINS_27OnePNCVolumeVariablesTraitsINS5_11FieldVectorIdLi4EEENS_12FluidSystems11OnePAdapterINS17_5H2ON2IdNS17_18H2ON2DefaultPolicyILb1EEEEELi0EEENS_24NonEquilibriumFluidStateIdS1D_EENS_12SolidSystems15InertSolidPhaseIdNS_10Components8ConstantILi1EdEEEENS_15InertSolidStateIdS1L_EEdNS_25NonEquilibriumModelTraitsINS_30OnePNCUnconstrainedModelTraitsINS_17OnePNCModelTraitsILi2ELb1ELi2EEEEELb0ELb1ELi1ELi1ELNS_18NusseltFormulationE1ELNS_19SherwoodFormulationE0EEEEENS_21OnePNCVolumeVariablesIS1W_EELb0ELb1ELi1EEEEELb0EEELb0EEERKNS_31CCTpfaElementFluxVariablesCacheINS_28CCTpfaGridFluxVariablesCacheIS12_NS_44PorousMediumFluxVariablesCacheImplementationIS3_LNS_20DiscretizationMethodE2EEENS_50PorousMediumFluxVariablesCacheFillerImplementationIS3_LS28_2EEELb0ENS_26CCTpfaDefaultGridFVCTraitsIS12_S29_S2B_EEEELb0EEERKNS_22CCElementBoundaryTypesE+0x341)[0x55c4b431c3e1]
[behandla:19637] [ 9] /data/build/dumux/test/porousmediumflow/1pnc/implicit/nonequilibrium/test_1p2c_nonequilibrium_tpfa(_ZNK5Dumux20FVLocalAssemblerBaseINS_10Properties4TTag35OnePTwoCThermalNonequilibriumCCTpfaENS_11FVAssemblerIS3_LNS_10DiffMethodE0ELb1EEENS_16CCLocalAssemblerIS3_S6_LS5_0ELb1EEELb1EE17evalLocalResidualEv+0xd6)[0x55c4b431ccb6]
[behandla:19637] [10] /data/build/dumux/test/porousmediumflow/1pnc/implicit/nonequilibrium/test_1p2c_nonequilibrium_tpfa(_ZN5Dumux16CCLocalAssemblerINS_10Properties4TTag35OnePTwoCThermalNonequilibriumCCTpfaENS_11FVAssemblerIS3_LNS_10DiffMethodE0ELb1EEELS5_0ELb1EE31assembleJacobianAndResidualImplERN4Dune10BCRSMatrixINS8_11FieldMatrixIdLi4ELi4EEESaISB_EEERNS_27NonEquilibriumGridVariablesIS3_EE+0x74d)[0x55c4b433ef4d]
[behandla:19637] [11] /data/build/dumux/test/porousmediumflow/1pnc/implicit/nonequilibrium/test_1p2c_nonequilibrium_tpfa(_ZNK5Dumux11FVAssemblerINS_10Properties4TTag35OnePTwoCThermalNonequilibriumCCTpfaELNS_10DiffMethodE0ELb1EE9assemble_IZNS5_27assembleJacobianAndResidualINS_18PartialReassemblerIS5_EEEEvRKN4Dune11BlockVectorINSA_11FieldVectorIdLi4EEESaISD_EEEPKT_EUlRKNSA_6EntityILi0ELi2EKNSA_8YaspGridILi2ENSA_22EquidistantCoordinatesIdLi2EEEEENSA_10YaspEntityEEEE_EEvOSI_+0x132)[0x55c4b4340b52]
[behandla:19637] [12] /data/build/dumux/test/porousmediumflow/1pnc/implicit/nonequilibrium/test_1p2c_nonequilibrium_tpfa(main+0xeb3)[0x55c4b4282c53]
[behandla:19637] [13] /lib/x86_64-linux-gnu/libc.so.6(__libc_start_main+0xe7)[0x7f3fc9066b97]
[behandla:19637] [14] /data/build/dumux/test/porousmediumflow/1pnc/implicit/nonequilibrium/test_1p2c_nonequilibrium_tpfa(_start+0x2a)[0x55c4b4286a2a]
[behandla:19637] *** End of error message ***
63/186 Test #63: test_1p2c_nonequilibrium_tpfa .....................***Failed 1.82 secTest command: /data/src/dumux/bin/testing/runtest.py "--script" "fuzzy" "--files" "/data/src/dumux/test/references/test_mpnc_kinetic_box-reference.vtu" "/data/build/dumux/test/porousmediumflow/mpnc/implicit/kinetic/test_mpnc_kinetic_box-00011.vtu" "--command" "/data/build/dumux/test/porousmediumflow/mpnc/implicit/kinetic/test_mpnc_kinetic_box params.input -Problem.Name test_mpnc_kinetic_box"
Test timeout computed to be: 300
Chuck Norris has successfully compiled DuMuX.
Reading parameters from file params.input.
The H2O-N2 fluid system was configured with the following policy:
- use H2O density as liquid mixture density: true
- use ideal gas density: true
- use N2 viscosity as gas mixture viscosity: true
- use N2 heat conductivity as gas mixture heat conductivity: true
- use ideal gas heat capacities: true
-------------------------------------------------------------------------
Initializing tables for the H2O fluid properties (10000 entries).
Temperature -> min: 2.780e+02, max: 4.531e+02, n: 100
Pressure -> min: 7.500e+04, max: 2.250e+05, n: 100
-------------------------------------------------------------------------
Writing output for problem "test_mpnc_kinetic_box". Took 6.039e-01 seconds.
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble/solve/update time: 1.278e+00(4.768e+01%)/1.402e+00(5.231e+01%)/3.405e-04(1.270e-02%)
Writing output for problem "test_mpnc_kinetic_box". Took 4.812e-02 seconds.
[ 1%] Time step 1 done in 2.736643 seconds. Wall clock time: 2.785, time: 0.05000, time step size: 0.05000000
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble/solve/update time: 0.95099143(48.46939834%)/1.01091940(51.52376100%)/0.00013422(0.00684067%)
Writing output for problem "test_mpnc_kinetic_box". Took 0.04853347 seconds.
[ 1%] Time step 2 done in 2.051791 seconds. Wall clock time: 4.837, time: 0.12500, time step size: 0.07500000
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble/solve/update time: 0.94914820(48.59345643%)/1.00394319(51.39879041%)/0.00015144(0.00775316%)
Writing output for problem "test_mpnc_kinetic_box". Took 0.04807224 seconds.
[ 2%] Time step 3 done in 2.043512 seconds. Wall clock time: 6.880, time: 0.24375, time step size: 0.11875000
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble/solve/update time: 0.95115055(48.39749146%)/1.01398697(51.59480356%)/0.00015143(0.00770497%)
Writing output for problem "test_mpnc_kinetic_box". Took 0.04845110 seconds.
[ 4%] Time step 4 done in 2.055532 seconds. Wall clock time: 8.936, time: 0.43177, time step size: 0.18802083
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble/solve/update time: 0.95967631(48.69862390%)/1.01083155(51.29448896%)/0.00013572(0.00688714%)
Writing output for problem "test_mpnc_kinetic_box". Took 0.04814657 seconds.
[ 7%] Time step 5 done in 2.060660 seconds. Wall clock time: 10.996, time: 0.72947, time step size: 0.29769965
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble/solve/update time: 1.26521772(48.89266931%)/1.32233187(51.09977040%)/0.00019564(0.00756029%)
Writing output for problem "test_mpnc_kinetic_box". Took 0.04806234 seconds.
[ 12%] Time step 6 done in 2.691426 seconds. Wall clock time: 13.688, time: 1.20083, time step size: 0.47135778
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble/solve/update time: 1.27771621(48.82405213%)/1.33907903(51.16884610%)/0.00018585(0.00710177%)
Writing output for problem "test_mpnc_kinetic_box". Took 0.04817870 seconds.
[ 19%] Time step 7 done in 2.720932 seconds. Wall clock time: 16.409, time: 1.90786, time step size: 0.70703668
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble/solve/update time: 1.27635560(48.32649627%)/1.36457241(51.66663862%)/0.00018132(0.00686511%)
Writing output for problem "test_mpnc_kinetic_box". Took 0.04837157 seconds.
[ 30%] Time step 8 done in 2.745505 seconds. Wall clock time: 19.154, time: 2.96842, time step size: 1.06055501
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble/solve/update time: 1.28703688(48.70908916%)/1.35506024(51.28349543%)/0.00019594(0.00741542%)
Writing output for problem "test_mpnc_kinetic_box". Took 0.04841897 seconds.
[ 46%] Time step 9 done in 2.747992 seconds. Wall clock time: 21.902, time: 4.55925, time step size: 1.59083252
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble/solve/update time: 1.27011454(48.08293266%)/1.37121299(51.91023325%)/0.00018052(0.00683409%)
Writing output for problem "test_mpnc_kinetic_box". Took 0.04838746 seconds.
[ 69%] Time step 10 done in 2.745616 seconds. Wall clock time: 24.648, time: 6.94550, time step size: 2.38624878
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble: r(x^k) = dS/dt + div F - q; M = grad r
Assemble/solve/update time: 1.27372658(48.61208584%)/1.34627708(51.38099319%)/0.00018134(0.00692096%)
Writing output for problem "test_mpnc_kinetic_box". Took 0.04840041 seconds.
[100%] Time step 11 done in 2.725102 seconds. Wall clock time: 27.373, time: 10.00000, time step size: 3.05449874
Simulation took 27.37315323 seconds on 1 processes.
The cumulative CPU time was 27.37315323 seconds.
# Runtime-specified parameters used:
[ BoundaryConditions ]
TInject = "293"
massFluxInjectedPhase = "0.75"
percentOfEquil = ".1"
[ Component ]
SolidDensity = "2600"
SolidHeatCapacity = "817"
SolidThermalConductivity = "3"
[ FluidSystem ]
nPressure = "100"
nTemperature = "100"
[ Grid ]
Cells0 = "14"
Cells1 = "15 15"
Grading0 = "1.0"
Grading1 = "-0.833333 0.833333"
Positions0 = "0.0 1.0"
Positions1 = "0.0 0.25 0.5"
[ InitialConditions ]
SwFFInitial = "1e-4"
SwPMInitial = "0.8"
TInitial = "293"
pnInitial = "1e5"
pnInjection = "100003"
[ Problem ]
Name = "test_mpnc_kinetic_box"
[ SpatialParams ]
[ SpatialParams.FreeFlow ]
meanPoreSize = "1e-2"
permeability = "1e-6"
porosity = "0.99"
[ SpatialParams.PorousMedium ]
factorEnergyTransfer = "1"
factorMassTransfer = "1"
meanPoreSize = "1e-4"
permeability = "1e-11"
porosity = "0.4"
[ SpatialParams.soil ]
BCPd = "2.290e+03"
BClambda = "2.740e+00"
Snr = "0"
Swr = "0"
aNonWettingSolidA1 = "1.369e+03"
aNonWettingSolidA2 = "-3.782e+00"
aNonWettingSolidA3 = "1.063e-09"
aWettingNonWettingA1 = "-1.603e-01"
aWettingNonWettingA2 = "1.429e-05"
aWettingNonWettingA3 = "1.915e-01"
[ TimeLoop ]
DtInitial = "0.05"
TEnd = "10"
[ Vtk ]
AddVelocity = "1"
# Global default parameters used:
[ Assembly ]
NumericDifferenceMethod = "1"
[ Flux ]
UpwindWeight = "1.0"
[ LinearSolver ]
MaxIterations = "250"
PreconditionerIterations = "1"
PreconditionerRelaxation = "1.0"
ResidualReduction = "1e-13"
Verbosity = "0"
[ Newton ]
EnableAbsoluteResidualCriterion = "false"
EnableChop = "false"
EnablePartialReassembly = "false"
EnableResidualCriterion = "false"
EnableShiftCriterion = "true"
MaxAbsoluteResidual = "1e-5"
MaxRelativeShift = "1e-8"
MaxSteps = "18"
ResidualReduction = "1e-5"
SatisfyResidualAndShiftCriterion = "false"
TargetSteps = "10"
UseLineSearch = "false"
[ Problem ]
EnableGravity = "true"
[ TimeLoop ]
MaxTimeStepSize = "1e300"
[ Vtk ]
AddProcessRank = "true"
# Unused parameters:
SpatialParams.soil.VGAlpha = "3.512e-04"
SpatialParams.soil.VGN = "4.716e+00"
SpatialParams.soil.specificSolidsurface = "4022.994"
SourceSink.heatIntoSolid = "0"
Constants.nRestart = "100"
FluidSystem.hammer = "1e4"
Chuck Norris has compiled DuMuX even two times in a row!
Fuzzy comparison...
Comparing /data/src/dumux/test/references/test_mpnc_kinetic_box-reference.vtu and /data/build/dumux/test/porousmediumflow/mpnc/implicit/kinetic/test_mpnc_kinetic_box-00011.vtu
... with a maximum relative error of 0.01 and a maximum absolute error of 1.5e-07*max_abs_parameter_value.
Data differs in parameter: velocity_gas (m/s)_1
Difference is too large: 8.70% -> between: 1.91128e-06 and 1.74495e-06
Info for velocity_gas (m/s)_1: max_abs_parameter_value=0.564606 and min_abs_parameter_value=1.74495e-06.
Data differs in parameter: velocity_liq (m/s)_0
Difference is too large: 1.00% -> between: 6.90209e-08 and 6.97191e-08
Info for velocity_liq (m/s)_0: max_abs_parameter_value=7.2564e-08 and min_abs_parameter_value=8.35171e-16.
Data differs in parameter: x^H2O_gas
Difference is too large: 55.46% -> between: 0.023197 and 0.0103322
Info for x^H2O_gas: max_abs_parameter_value=0.0232059 and min_abs_parameter_value=0.00232059.
Data differs in parameter: x^N2_gas
Difference is too large: 1.30% -> between: 0.976803 and 0.989668
Info for x^N2_gas: max_abs_parameter_value=0.997679 and min_abs_parameter_value=0.976794.
Test #155: test_mpnc_kinetic_box .............................***Failed 29.19 sec