Authorization required, but no authorization protocol specified Authorization required, but no authorization protocol specified Authorization required, but no authorization protocol specified Authorization required, but no authorization protocol specified Authorization required, but no authorization protocol specified Authorization required, but no authorization protocol specified Authorization required, but no authorization protocol specified Authorization required, but no authorization protocol specified Authorization required, but no authorization protocol specified Authorization required, but no authorization protocol specified /*---------------------------------------------------------------------------*\ ========= | \\ / F ield | OpenFOAM: The Open Source CFD Toolbox \\ / O peration | Website: https://openfoam.org \\ / A nd | Version: 13 \\/ M anipulation | \*---------------------------------------------------------------------------*/ Build : 13-65eda17ad4ca Exec : foamRun -parallel Date : Jul 11 2025 Time : 16:38:47 Host : "franco-work" PID : 2770839 I/O : uncollated Case : /home/franco/Downloads/bubbleColumn2kV13 nProcs : 8 Slaves : 7 ( "franco-work.2770840" "franco-work.2770841" "franco-work.2770842" "franco-work.2770843" "franco-work.2770844" "franco-work.2770845" "franco-work.2770846" ) Pstream initialised with: floatTransfer : false nProcsSimpleSum : 0 commsType : nonBlocking polling iterations : 0 sigFpe : Enabling floating point exception trapping (FOAM_SIGFPE). fileModificationChecking : Monitoring run-time modified files using timeStampMaster (fileModificationSkew 10) allowSystemOperations : Allowing user-supplied system call operations // * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * * // Create time Create mesh for time = 0 Selecting solver multiphaseEuler No MRF models present Selecting phaseModel for gas: multicomponentIsothermalPhaseModel Selecting diameterModel for phase gas: velocityGroup Selecting thermodynamics package { type heRhoThermo; mixture multicomponentMixture; transport const; thermo eConst; equationOfState perfectGas; specie specie; energy sensibleInternalEnergy; } Calculating face flux field phi.gas Selecting turbulence model type laminar Selecting laminar stress model Stokes Selecting thermophysical transport type laminar Selecting default laminar thermophysical transport model unityLewisFourier Selecting phaseModel for liquid: multicomponentIsothermalPhaseModel Selecting diameterModel for phase liquid: constant Selecting thermodynamics package { type heRhoThermo; mixture multicomponentMixture; transport const; thermo eConst; equationOfState rPolynomial; specie specie; energy sensibleInternalEnergy; } Calculating face flux field phi.liquid Selecting turbulence model type laminar Selecting laminar stress model Stokes Selecting thermophysical transport type laminar Selecting default laminar thermophysical transport model unityLewisFourier Selecting surfaceTensionCoefficientModel for gas_liquid: constant Selecting dragModel blending method for gas_liquid: linear Selecting dragModel for gas_dispersedIn_liquid: TomiyamaCorrelatedOrlando Selecting dragModel for liquid_dispersedIn_gas: SchillerNaumann Selecting virtualMassModel blending method for gas_liquid: linear Selecting virtualMassModel for gas_dispersedIn_liquid: constantCoefficient Selecting virtualMassModel for liquid_dispersedIn_gas: constantCoefficient Selecting SidedInterfacialModel blending method for gas_liquid: linear Selecting heatTransferModel for gas_dispersedIn_liquid_inThe_gas: RanzMarshall Selecting heatTransferModel for gas_dispersedIn_liquid_inThe_liquid: RanzMarshall Selecting heatTransferModel for liquid_dispersedIn_gas_inThe_gas: RanzMarshall Selecting heatTransferModel for liquid_dispersedIn_gas_inThe_liquid: RanzMarshall Setting up population balance: bubbles Selecting coalescence model for bubbles: Luo Selecting binary breakup model for bubbles: powerLawUniformBinary Courant Number mean: 6.01596e-07 max: 0.00692706 Creating fvModels from "constant/fvModels" Selecting finite volume model type massDiffusionLimitedPhaseChange Name: phaseChange Selecting interfaceCompositionModel for gas_liquid_inThe_gas: saturated Selecting saturationPressureModel ArdenBuck Selecting interfaceCompositionModel for gas_liquid_inThe_liquid: Henry Selecting SidedInterfacialModel blending method for gas_liquid: linear Selecting diffusiveMassTransferModel for gas_dispersedIn_liquid_inThe_gas: spherical Selecting diffusiveMassTransferModel for gas_dispersedIn_liquid_inThe_liquid: Frossling Selecting diffusiveMassTransferModel for liquid_dispersedIn_gas_inThe_gas: Frossling Selecting diffusiveMassTransferModel for liquid_dispersedIn_gas_inThe_liquid: spherical Selecting finite volume model type porosityForce Name: filter1 Porosity region filter1: selecting model: DarcyForchheimer creating porous zone: filter Creating fvConstraints from "system/fvConstraints" Selecting finite volume constraint type limitPressure Name: limitp min 10000 PIMPLE: No convergence criteria found PIMPLE: No corrector convergence criteria found Calculations will do 3 corrections PIMPLE: Operating solver in transient mode with 3 outer correctors Using dynamicCode for coded updateO2liquid at line 21 in "/home/franco/Downloads/bubbleColumn2kV13/system/functions/updateO2liquid" Creating new library in "dynamicCode/updateO2liquid/platforms/linux64GccDPInt32Opt/lib/libupdateO2liquid_c17dcb57373e4b2172a83a2f7ecc9882db24442e.so" "/opt/openfoam13/etc/codeTemplates/dynamicCode/codedFunctionObjectTemplate.C" "/home/franco/Downloads/bubbleColumn2kV13/dynamicCode/updateO2liquid/codedFunctionObjectTemplate.C" "/opt/openfoam13/etc/codeTemplates/dynamicCode/codedFunctionObjectTemplate.H" "/home/franco/Downloads/bubbleColumn2kV13/dynamicCode/updateO2liquid/codedFunctionObjectTemplate.H" Invoking "wmake -s libso /home/franco/Downloads/bubbleColumn2kV13/dynamicCode/updateO2liquid" wmake libso /home/franco/Downloads/bubbleColumn2kV13/dynamicCode/updateO2liquid ln: ./lnInclude wmkdep: codedFunctionObjectTemplate.C Ctoo: codedFunctionObjectTemplate.C ld: /home/franco/Downloads/bubbleColumn2kV13/dynamicCode/updateO2liquid/../platforms/linux64GccDPInt32Opt/lib/libupdateO2liquid_c17dcb57373e4b2172a83a2f7ecc9882db24442e.so Using dynamicCode for coded alphaSpecie at line 63 in "/home/franco/Downloads/bubbleColumn2kV13/system/functions/alphaSpecie" Creating new library in "dynamicCode/alphaSpecie/platforms/linux64GccDPInt32Opt/lib/libalphaSpecie_be4922a4fbb586e4fbf5878a3cca29e3c7f0506e.so" "/opt/openfoam13/etc/codeTemplates/dynamicCode/codedFunctionObjectTemplate.C" "/home/franco/Downloads/bubbleColumn2kV13/dynamicCode/alphaSpecie/codedFunctionObjectTemplate.C" "/opt/openfoam13/etc/codeTemplates/dynamicCode/codedFunctionObjectTemplate.H" "/home/franco/Downloads/bubbleColumn2kV13/dynamicCode/alphaSpecie/codedFunctionObjectTemplate.H" Invoking "wmake -s libso /home/franco/Downloads/bubbleColumn2kV13/dynamicCode/alphaSpecie" wmake libso /home/franco/Downloads/bubbleColumn2kV13/dynamicCode/alphaSpecie ln: ./lnInclude wmkdep: codedFunctionObjectTemplate.C Ctoo: codedFunctionObjectTemplate.C ld: /home/franco/Downloads/bubbleColumn2kV13/dynamicCode/alphaSpecie/../platforms/linux64GccDPInt32Opt/lib/libalphaSpecie_be4922a4fbb586e4fbf5878a3cca29e3c7f0506e.so Starting time loop [franco-work:2770840] *** An error occurred in MPI_Recv [franco-work:2770840] *** reported by process [3799580673,1] [franco-work:2770840] *** on communicator MPI COMMUNICATOR 3 SPLIT FROM 0 [franco-work:2770840] *** MPI_ERR_TRUNCATE: message truncated [franco-work:2770840] *** MPI_ERRORS_ARE_FATAL (processes in this communicator will now abort, [franco-work:2770840] *** and potentially your MPI job) [franco-work:2770825] 2 more processes have sent help message help-mpi-errors.txt / mpi_errors_are_fatal [franco-work:2770825] Set MCA parameter "orte_base_help_aggregate" to 0 to see all help / error messages