|
[Sponsors] |
ansys cfx solver exit with return code 1!!!!! |
|
LinkBack | Thread Tools | Search this Thread | Display Modes |
August 16, 2013, 12:45 |
ansys cfx solver exit with return code 1!!!!!
|
#1 |
New Member
mhabibnia
Join Date: Jun 2013
Posts: 6
Rep Power: 13 |
hi, i'm using ansys transient structural and cfx coupling to analyse a two way fsi problem in a free surface flow condition, but when cfx solver starts the run, in the beginnig this error comes up and no result files will be created:
The ANSYS CFX solver exited with return code 1. No results file has been created. for the record, i'm analysing a circular column in water, can anybody help me please? |
|
August 16, 2013, 13:29 |
|
#2 |
Senior Member
Mr CFD
Join Date: Jun 2012
Location: Britain
Posts: 361
Rep Power: 15 |
Post the .out file and read the FAQ.
|
|
August 16, 2013, 15:05 |
|
#3 |
New Member
mhabibnia
Join Date: Jun 2013
Posts: 6
Rep Power: 13 |
here is the out file
|
|
August 16, 2013, 16:42 |
|
#4 |
Senior Member
Mr CFD
Join Date: Jun 2012
Location: Britain
Posts: 361
Rep Power: 15 |
Can you just simply copy and paste the text in here?
Besides that .zip file does not work anyway. Also what simulations are you doing exactly? You're not exactly spoon feeding us the information we need for us to help you! |
|
August 16, 2013, 23:40 |
|
#5 |
New Member
mhabibnia
Join Date: Jun 2013
Posts: 6
Rep Power: 13 |
ok here we go, in the structural part, earthquake acceleration is given to the columns bottom; in cfx part, we have a two phase (air and water) domain to show the depth of water the column is in, and of course it is coupled to the structural, below is the full out file:
This run of the CFX-14.0 Solver started at 22:24:37 on 16 Aug 2013 by user amir on AMIR-PC (intel_xeon64.sse2_winnt) using the command: "E:\ANSYS Inc\v140\CFX\bin\perllib\cfx5solve.pl" -batch -ccl runInput.ccl -fullname "Fluid Flow CFX_001" Setting up CFX Solver run ... +--------------------------------------------------------------------+ | | | Processing ANSYS Input File (Running CCL2MF) | | | +--------------------------------------------------------------------+ Created C:\Users\amir\Desktop\work\01_pending_tasks\dp0_CF X_Solution_1\Fluid Flow CFX_001.ansys\ANSYS.mf +--------------------------------------------------------------------+ | | | Starting ANSYS Solver | | | +--------------------------------------------------------------------+ +--------------------------------------------------------------------+ | | | CFX Command Language for Run | | | +--------------------------------------------------------------------+ LIBRARY: CEL: EXPRESSIONS: a = step((y-uph)/1[m]) uph = 9 [m] wat = 1-a END END MATERIAL: Air at 25 C Material Description = Air at 25 C and 1 atm (dry) Material Group = Air Data, Constant Property Gases Option = Pure Substance Thermodynamic State = Gas PROPERTIES: Option = General Material EQUATION OF STATE: Density = 1.185 [kg m^-3] Molar Mass = 28.96 [kg kmol^-1] Option = Value END SPECIFIC HEAT CAPACITY: Option = Value Specific Heat Capacity = 1.0044E+03 [J kg^-1 K^-1] Specific Heat Type = Constant Pressure END REFERENCE STATE: Option = Specified Point Reference Pressure = 1 [atm] Reference Specific Enthalpy = 0. [J/kg] Reference Specific Entropy = 0. [J/kg/K] Reference Temperature = 25 [C] END DYNAMIC VISCOSITY: Dynamic Viscosity = 1.831E-05 [kg m^-1 s^-1] Option = Value END THERMAL CONDUCTIVITY: Option = Value Thermal Conductivity = 2.61E-02 [W m^-1 K^-1] END ABSORPTION COEFFICIENT: Absorption Coefficient = 0.01 [m^-1] Option = Value END SCATTERING COEFFICIENT: Option = Value Scattering Coefficient = 0.0 [m^-1] END REFRACTIVE INDEX: Option = Value Refractive Index = 1.0 [m m^-1] END THERMAL EXPANSIVITY: Option = Value Thermal Expansivity = 0.003356 [K^-1] END END END MATERIAL: Water Material Description = Water (liquid) Material Group = Water Data, Constant Property Liquids Option = Pure Substance Thermodynamic State = Liquid PROPERTIES: Option = General Material EQUATION OF STATE: Density = 997.0 [kg m^-3] Molar Mass = 18.02 [kg kmol^-1] Option = Value END SPECIFIC HEAT CAPACITY: Option = Value Specific Heat Capacity = 4181.7 [J kg^-1 K^-1] Specific Heat Type = Constant Pressure END REFERENCE STATE: Option = Specified Point Reference Pressure = 1 [atm] Reference Specific Enthalpy = 0.0 [J/kg] Reference Specific Entropy = 0.0 [J/kg/K] Reference Temperature = 25 [C] END DYNAMIC VISCOSITY: Dynamic Viscosity = 8.899E-4 [kg m^-1 s^-1] Option = Value END THERMAL CONDUCTIVITY: Option = Value Thermal Conductivity = 0.6069 [W m^-1 K^-1] END ABSORPTION COEFFICIENT: Absorption Coefficient = 1.0 [m^-1] Option = Value END SCATTERING COEFFICIENT: Option = Value Scattering Coefficient = 0.0 [m^-1] END REFRACTIVE INDEX: Option = Value Refractive Index = 1.0 [m m^-1] END THERMAL EXPANSIVITY: Option = Value Thermal Expansivity = 2.57E-04 [K^-1] END END END END FLOW: Flow Analysis 1 SOLUTION UNITS: Angle Units = [rad] Length Units = [m] Mass Units = [kg] Solid Angle Units = [sr] Temperature Units = [K] Time Units = [s] END ANALYSIS TYPE: Option = Transient EXTERNAL SOLVER COUPLING: ANSYS Input File = ds.dat Option = ANSYS MultiField COUPLING TIME CONTROL: COUPLING INITIAL TIME: Option = Automatic END COUPLING TIME DURATION: Option = Total Time Total Time = 1 [s] END COUPLING TIME STEPS: Option = Timesteps Timesteps = 0.01 [s] END END END INITIAL TIME: Option = Coupling Initial Time END TIME DURATION: Option = Coupling Time Duration END TIME STEPS: Option = Coupling Timesteps END END DOMAIN: Default Domain Coord Frame = Coord 0 Domain Type = Fluid Location = B26 BOUNDARY: Default Domain Default Boundary Type = WALL Location = F20.26,F21.26,F22.26,F24.26 BOUNDARY CONDITIONS: MASS AND MOMENTUM: Option = No Slip Wall END MESH MOTION: Option = Stationary END WALL ROUGHNESS: Option = Smooth Wall END END END BOUNDARY: in Boundary Type = INLET Location = F23.26 BOUNDARY CONDITIONS: FLOW REGIME: Option = Subsonic END MASS AND MOMENTUM: Normal Speed = 0 [m s^-1] Option = Normal Speed END MESH MOTION: Option = Stationary END TURBULENCE: Option = Medium Intensity and Eddy Viscosity Ratio END END FLUID: air BOUNDARY CONDITIONS: VOLUME FRACTION: Option = Value Volume Fraction = a END END END FLUID: water BOUNDARY CONDITIONS: VOLUME FRACTION: Option = Value Volume Fraction = wat END END END END BOUNDARY: interface Boundary Type = WALL Location = F25.26 BOUNDARY CONDITIONS: MASS AND MOMENTUM: Option = No Slip Wall END MESH MOTION: ANSYS Interface = FSIN_1 Option = ANSYS MultiField Receive from ANSYS = Total Mesh Displacement Send to ANSYS = Total Force END WALL ROUGHNESS: Option = Smooth Wall END END END BOUNDARY: top Boundary Type = OPENING Location = F27.26 BOUNDARY CONDITIONS: FLOW REGIME: Option = Subsonic END MASS AND MOMENTUM: Option = Entrainment Relative Pressure = 0 [Pa] END MESH MOTION: Option = Stationary END TURBULENCE: Option = Zero Gradient END END FLUID: air BOUNDARY CONDITIONS: VOLUME FRACTION: Option = Value Volume Fraction = 1 END END END FLUID: water BOUNDARY CONDITIONS: VOLUME FRACTION: Option = Value Volume Fraction = 0 END END END END DOMAIN MODELS: BUOYANCY MODEL: Buoyancy Reference Density = 1.185 [kg m^-3] Gravity X Component = 0 [m s^-2] Gravity Y Component = -g Gravity Z Component = 0 [m s^-2] Option = Buoyant BUOYANCY REFERENCE LOCATION: Option = Automatic END END DOMAIN MOTION: Option = Stationary END MESH DEFORMATION: Option = Regions of Motion Specified MESH MOTION MODEL: Option = Displacement Diffusion MESH STIFFNESS: Option = Increase near Small Volumes Stiffness Model Exponent = 10 END END END REFERENCE PRESSURE: Reference Pressure = 1 [atm] END END FLUID DEFINITION: air Material = Air at 25 C Option = Material Library MORPHOLOGY: Option = Continuous Fluid END END FLUID DEFINITION: water Material = Water Option = Material Library MORPHOLOGY: Option = Continuous Fluid END END FLUID MODELS: COMBUSTION MODEL: Option = None END FLUID: air FLUID BUOYANCY MODEL: Option = Density Difference END END FLUID: water FLUID BUOYANCY MODEL: Option = Density Difference END END HEAT TRANSFER MODEL: Fluid Temperature = 25 [C] Homogeneous Model = True Option = Isothermal END THERMAL RADIATION MODEL: Option = None END TURBULENCE MODEL: Option = k epsilon BUOYANCY TURBULENCE: Option = None END END TURBULENT WALL FUNCTIONS: Option = Scalable END END FLUID PAIR: air | water INTERPHASE TRANSFER MODEL: Option = None END MASS TRANSFER: Option = None END SURFACE TENSION MODEL: Option = None END END MULTIPHASE MODELS: Homogeneous Model = On FREE SURFACE MODEL: Option = Standard END END END INITIALISATION: Option = Automatic FLUID: air INITIAL CONDITIONS: VOLUME FRACTION: Option = Automatic with Value Volume Fraction = a END END END FLUID: water INITIAL CONDITIONS: VOLUME FRACTION: Option = Automatic with Value Volume Fraction = wat END END END INITIAL CONDITIONS: Velocity Type = Cartesian CARTESIAN VELOCITY COMPONENTS: Option = Automatic with Value U = 0 [m s^-1] V = 0 [m s^-1] W = 0 [m s^-1] END STATIC PRESSURE: Option = Automatic with Value Relative Pressure = 0 [Pa] END TURBULENCE INITIAL CONDITIONS: Option = Medium Intensity and Eddy Viscosity Ratio END END END OUTPUT CONTROL: RESULTS: File Compression Level = Default Option = Standard END END SOLVER CONTROL: Turbulence Numerics = First Order ADVECTION SCHEME: Option = Upwind END CONVERGENCE CONTROL: Maximum Number of Coefficient Loops = 3 Minimum Number of Coefficient Loops = 1 Timescale Control = Coefficient Loops END CONVERGENCE CRITERIA: Residual Target = 1.E-4 Residual Type = RMS END EXTERNAL SOLVER COUPLING CONTROL: COUPLING DATA TRANSFER CONTROL: Convergence Target = 1e-2 Under Relaxation Factor = 0.75 END COUPLING STEP CONTROL: Maximum Number of Coupling Iterations = 10 Minimum Number of Coupling Iterations = 1 SOLUTION SEQUENCE CONTROL: Solve ANSYS Fields = Before CFX Fields END END END |
|
August 16, 2013, 23:41 |
|
#6 |
New Member
mhabibnia
Join Date: Jun 2013
Posts: 6
Rep Power: 13 |
MULTIPHASE CONTROL:
Volume Fraction Coupling = Coupled END TRANSIENT SCHEME: Option = First Order Backward Euler END END END COMMAND FILE: Version = 14.0 Results Version = 14.0 END SIMULATION CONTROL: EXECUTION CONTROL: EXECUTABLE SELECTION: Double Precision = Off END INTERPOLATOR STEP CONTROL: Runtime Priority = Standard MEMORY CONTROL: Memory Allocation Factor = 1.0 END END MFX RUN CONTROL: MFX RUN DEFINITION: MFX Run Mode = Start ANSYS and CFX Process ANSYS Input File = On Restart ANSYS Run = Off END MFX SOLVER CONTROL: ANSYS Installation Root = E:\ANSYS Inc\v140\ansys END END PARALLEL HOST LIBRARY: HOST DEFINITION: amirpc Remote Host Name = AMIR-PC Host Architecture String = winnt-amd64 Installation Root = E:\ANSYS Inc\v%v\CFX END END PARTITIONER STEP CONTROL: Multidomain Option = Independent Partitioning Runtime Priority = Standard EXECUTABLE SELECTION: Use Large Problem Partitioner = Off END MEMORY CONTROL: Memory Allocation Factor = 1.0 END PARTITIONING TYPE: MeTiS Type = k-way Option = MeTiS Partition Size Rule = Automatic END END RUN DEFINITION: Run Mode = Full Solver Input File = Fluid Flow CFX.def END SOLVER STEP CONTROL: Runtime Priority = Standard MEMORY CONTROL: Memory Allocation Factor = 1.0 END PARALLEL ENVIRONMENT: Number of Processes = 1 Start Method = Serial END PROCESS COUPLING: Process Name = CFX Host Port = 52438 Host Name = AMIR-PC END END END END +--------------------------------------------------------------------+ | | | Solver | | | +--------------------------------------------------------------------+ +--------------------------------------------------------------------+ | | | ANSYS(R) CFX(R) Solver 14.0 | | | | Version 2011.10.10-23.01 Tue Oct 11 00:28:38 GMTDT 2011 | | | | Executable Attributes | | | | single-int32-64bit-novc8-noifort-novc6-optimised-supfort-noprof-nos| | | | (C) 2011 ANSYS, Inc. | | | | All rights reserved. Unauthorized use, distribution or duplication | | is prohibited. This product is subject to U.S. laws governing | | export and re-export. For full Legal Notice, see documentation. | +--------------------------------------------------------------------+ +--------------------------------------------------------------------+ | Job Information | +--------------------------------------------------------------------+ Run mode: serial run Host computer: AMIR-PC (PID:18568) Job started: Fri Aug 16 22:24:50 2013 Connecting to the following master process: Host Name : AMIR-PC Port Number : 52438 License Cap: ANSYS CFX Solver (Max 128K Nodes) License ID: AMIR-PC-SYSTEM-1620-011915 +--------------------------------------------------------------------+ | Memory Allocated for Run (Actual usage may be less) | +--------------------------------------------------------------------+ Data Type Kwords Words/Node Words/Elem Kbytes Bytes/Node Real 35111.7 8991.47 10972.40 137155.0 35965.88 Integer 1859.1 476.08 580.96 7262.0 1904.31 Character 3791.4 970.91 1184.81 3702.5 970.91 Logical 80.0 20.49 25.00 312.5 81.95 Double 56.4 14.44 17.62 440.6 115.54 +--------------------------------------------------------------------+ | Mesh Statistics | +--------------------------------------------------------------------+ | Domain Name | Orthog. Angle | Exp. Factor | Aspect Ratio | +----------------------+---------------+--------------+--------------+ | | Minimum [deg] | Maximum | Maximum | +----------------------+---------------+--------------+--------------+ | Default Domain | 67.5 OK | 3 OK | 4 OK | +----------------------+---------------+--------------+--------------+ | | %! %ok %OK | %! %ok %OK | %! %ok %OK | +----------------------+---------------+--------------+--------------+ | Default Domain | 0 0 100 | 0 0 100 | 0 0 100 | +----------------------+---------------+--------------+--------------+ Domain Name : Default Domain Total Number of Nodes = 3905 Total Number of Elements = 3200 Total Number of Prisms = 40 Total Number of Hexahedrons = 3160 Total Number of Faces = 1380 +--------------------------------------------------------------------+ | Buoyancy Reference Information | +--------------------------------------------------------------------+ Domain Group: Default Domain Buoyancy has been activated. The absolute pressure will include hydrostatic pressure contribution, using the following reference coordinates: ( 2.91154E-01, 1.00000E+01, 3.73309E-02). +--------------------------------------------------------------------+ | Initial Conditions Supplied by Fields in the Input Files | +--------------------------------------------------------------------+ Domain Name : Default Domain Mesh Coordinates +--------------------------------------------------------------------+ | Average Scale Information | +--------------------------------------------------------------------+ Domain Name : Default Domain Global Length = 1.4285E+01 Minimum Extent = 1.0000E+01 Maximum Extent = 1.7970E+01 water.Density = 9.9700E+02 water.Dynamic Viscosity = 8.8990E-04 water.Velocity = 0.0000E+00 water.Mass (Conservative) = 2.6155E+06 water.Mass (Normalised) = 2.6155E+06 water.Volume = 2.6233E+03 water.Volume Fraction = 9.0000E-01 air.Density = 1.1850E+00 air.Dynamic Viscosity = 1.8310E-05 air.Velocity = 0.0000E+00 air.Mass (Conservative) = 3.4541E+02 air.Mass (Normalised) = 3.4541E+02 air.Volume = 2.9148E+02 air.Volume Fraction = 1.0000E-01 Wave Speed = 1.1836E+01 Froude Number = 0.0000E+00 +--------------------------------------------------------------------+ | Boundary Condition Data Supplied by External Solver Coupling | +--------------------------------------------------------------------+ ANSYS Multi-field Solver : ANSYS CFX Boundary : interface CFX Variable : Total Mesh Displacement ANSYS Interface : 1 ANSYS Variable : DISP +--------------------------------------------------------------------+ | Checking for Isolated Fluid Regions | +--------------------------------------------------------------------+ No isolated fluid regions were found. +--------------------------------------------------------------------+ | The Equations Solved in This Calculation | +--------------------------------------------------------------------+ Subsystem : Mesh Displacement X-Disp Y-Disp Z-Disp Subsystem : Momentum and Mass U-Mom-Bulk V-Mom-Bulk W-Mom-Bulk VF-Constraint Mass-water Mass-air Subsystem : TurbKE and Diss.K K-TurbKE-Bulk E-Diss.K-Bulk CFD Solver started: Fri Aug 16 22:24:53 2013 +--------------------------------------------------------------------+ | Convergence History | +--------------------------------------------------------------------+ ================================================== ==================== | Timestepping Information | ---------------------------------------------------------------------- | Timestep | RMS Courant Number | Max Courant Number | +----------------------+----------------------+----------------------+ | 1.0000E-02 | 0.00 | 0.00 | ---------------------------------------------------------------------- ================================================== ==================== TIME STEP = 1 SIMULATION TIME = 1.0000E-02 CPU SECONDS = 3.627E+00 ---------------------------------------------------------------------- | COUPLING/STAGGER ITERATION = 1 | ---------------------------------------------------------------------- | SOLVING : Mesh Displacement | ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | X-Disp | 0.00 | 0.0E+00 | 0.0E+00 | 0.0E+00 OK| | Y-Disp | 0.00 | 0.0E+00 | 0.0E+00 | 0.0E+00 OK| | Z-Disp | 0.00 | 0.0E+00 | 0.0E+00 | 10.6 0.0E+00 OK| +----------------------+------+---------+---------+------------------+ +--------------------------------------------------------------------+ | Mesh Statistics | +--------------------------------------------------------------------+ | Domain Name | Orthog. Angle | Exp. Factor | Aspect Ratio | +----------------------+---------------+--------------+--------------+ | | Minimum [deg] | Maximum | Maximum | +----------------------+---------------+--------------+--------------+ | Default Domain | 67.5 OK | 3 OK | 4 OK | +----------------------+---------------+--------------+--------------+ | | %! %ok %OK | %! %ok %OK | %! %ok %OK | +----------------------+---------------+--------------+--------------+ | Default Domain | 0 0 100 | 0 0 100 | 0 0 100 | +----------------------+---------------+--------------+--------------+ ---------------------------------------------------------------------- COEFFICIENT LOOP ITERATION = 1 CPU SECONDS = 3.774E+00 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom-Bulk | 0.00 | 0.0E+00 | 0.0E+00 | 0.0E+00 OK| | V-Mom-Bulk | 0.00 | 1.9E-02 | 6.2E-02 | 1.2E-02 ok| | W-Mom-Bulk | 0.00 | 0.0E+00 | 0.0E+00 | 0.0E+00 OK| | Mass-water | 0.00 | 1.3E-04 | 4.6E-04 | 5.7E-01 ok| | Mass-air | 0.00 | 1.2E-04 | 3.8E-04 | 8.6 3.3E+00 F | +----------------------+------+---------+---------+------------------+ | K-TurbKE-Bulk | 0.00 | 3.1E-02 | 9.8E-01 | 11.2 2.3E-08 OK| | E-Diss.K-Bulk | 0.00 | 2.2E-02 | 1.0E+00 | 9.4 2.8E-08 OK| +----------------------+------+---------+---------+------------------+ ---------------------------------------------------------------------- COEFFICIENT LOOP ITERATION = 2 CPU SECONDS = 4.531E+00 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom-Bulk | 0.00 | 1.2E-03 | 4.3E-02 | 4.5E+01 F | | V-Mom-Bulk | 0.02 | 3.4E-04 | 1.2E-02 | 8.6E+00 F | | W-Mom-Bulk | 0.00 | 2.1E-03 | 1.1E-01 | 4.5E+01 F | | Mass-water | 0.02 | 2.3E-06 | 6.6E-05 | 1.6E+01 F | | Mass-air | 0.02 | 1.9E-06 | 4.4E-05 | 8.6 2.5E+01 F | +----------------------+------+---------+---------+------------------+ | K-TurbKE-Bulk | 0.83 | 2.5E-02 | 7.2E-01 | 11.0 4.2E-08 OK| | E-Diss.K-Bulk | 0.76 | 1.7E-02 | 1.0E+00 | 9.4 5.0E-07 OK| +----------------------+------+---------+---------+------------------+ ---------------------------------------------------------------------- COEFFICIENT LOOP ITERATION = 3 CPU SECONDS = 5.079E+00 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom-Bulk |13.10 | 1.5E-02 | 4.5E-01 | 6.2E-03 OK| | V-Mom-Bulk |29.20 | 1.0E-02 | 3.9E-01 | 1.3E-03 OK| | W-Mom-Bulk | 7.86 | 1.6E-02 | 4.6E-01 | 1.3E-03 OK| | Mass-water |99.99 | 9.5E-04 | 3.5E-02 | 4.3E-01 ok| | Mass-air |99.99 | 1.2E-03 | 5.2E-02 | 16.3 1.2E+00 F | +----------------------+------+---------+---------+------------------+ | K-TurbKE-Bulk | 0.27 | 6.8E-03 | 4.0E-01 | 10.2 9.9E-02 OK| | E-Diss.K-Bulk | 2.52 | 4.3E-02 | 1.0E+00 | 17.3 3.2E-02 OK| +----------------------+------+---------+---------+------------------+ ---------------------------------------------------------------------- | COUPLING/STAGGER ITERATION = 2 | ---------------------------------------------------------------------- | SOLVING : Mesh Displacement | ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | X-Disp | 0.00 | 9.5E-04 | 8.6E-03 | 2.2E-08 OK| | Y-Disp | 0.00 | 7.1E-04 | 4.9E-03 | 2.1E-08 OK| | Z-Disp | 0.00 | 2.9E-03 | 2.4E-02 | 10.6 2.2E-08 OK| +----------------------+------+---------+---------+------------------+ | X-Disp | 0.04 | 4.1E-05 | 5.2E-04 | 4.4E-05 OK| | Y-Disp | 0.07 | 4.8E-05 | 4.2E-04 | 3.1E-06 OK| | Z-Disp | 0.05 | 1.3E-04 | 1.7E-03 | 10.6 5.3E-05 OK| +----------------------+------+---------+---------+------------------+ | X-Disp | 0.23 | 9.5E-06 | 9.8E-05 | 9.3E-05 OK| | Y-Disp | 0.26 | 1.3E-05 | 1.4E-04 | 1.6E-05 OK| | Z-Disp | 0.24 | 3.0E-05 | 3.0E-04 | 10.6 3.3E-04 OK| +----------------------+------+---------+---------+------------------+ +--------------------------------------------------------------------+ | Mesh Statistics | +--------------------------------------------------------------------+ | Domain Name | Orthog. Angle | Exp. Factor | Aspect Ratio | +----------------------+---------------+--------------+--------------+ | | Minimum [deg] | Maximum | Maximum | +----------------------+---------------+--------------+--------------+ | Default Domain | 67.5 OK | 3 OK | 4 OK | +----------------------+---------------+--------------+--------------+ | | %! %ok %OK | %! %ok %OK | %! %ok %OK | +----------------------+---------------+--------------+--------------+ | Default Domain | 0 0 100 | 0 0 100 | 0 0 100 | +----------------------+---------------+--------------+--------------+ |
|
August 16, 2013, 23:41 |
|
#7 |
New Member
mhabibnia
Join Date: Jun 2013
Posts: 6
Rep Power: 13 |
----------------------------------------------------------------------
COEFFICIENT LOOP ITERATION = 4 CPU SECONDS = 6.412E+00 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom-Bulk | 2.02 | 3.1E-02 | 9.0E-01 | 7.8E-01 ok| | V-Mom-Bulk | 1.08 | 1.1E-02 | 4.4E-01 | 1.8E-01 ok| | W-Mom-Bulk | 2.51 | 4.1E-02 | 1.4E+00 | 4.2E-01 ok| | Mass-water | 0.15 | 1.4E-04 | 6.0E-03 | 9.6E-01 ok| | Mass-air | 0.11 | 1.3E-04 | 5.7E-03 | 8.6 6.0E-01 ok| +----------------------+------+---------+---------+------------------+ | K-TurbKE-Bulk | 9.66 | 6.6E-02 | 8.1E-01 | 10.3 3.1E-08 OK| | E-Diss.K-Bulk | 1.01 | 4.3E-02 | 7.3E-01 | 17.5 3.0E-08 OK| +----------------------+------+---------+---------+------------------+ ---------------------------------------------------------------------- COEFFICIENT LOOP ITERATION = 5 CPU SECONDS = 6.996E+00 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom-Bulk | 0.03 | 9.1E-04 | 1.8E-02 | 7.6E+00 F | | V-Mom-Bulk | 0.04 | 4.1E-04 | 1.0E-02 | 4.6E-01 ok| | W-Mom-Bulk | 0.02 | 1.0E-03 | 2.6E-02 | 1.4E+01 F | | Mass-water | 0.00 | 4.9E-07 | 1.2E-05 | 4.4E+00 F | | Mass-air | 0.00 | 2.0E-07 | 8.0E-06 | 8.6 3.6E+01 F | +----------------------+------+---------+---------+------------------+ | K-TurbKE-Bulk | 0.45 | 2.9E-02 | 7.2E-01 | 10.7 7.1E-06 OK| | E-Diss.K-Bulk | 0.52 | 2.2E-02 | 1.0E+00 |100.3 7.8E-08 OK| +----------------------+------+---------+---------+------------------+ ---------------------------------------------------------------------- COEFFICIENT LOOP ITERATION = 6 CPU SECONDS = 7.577E+00 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom-Bulk |23.29 | 2.1E-02 | 6.9E-01 | 2.6E-03 OK| | V-Mom-Bulk |29.12 | 1.2E-02 | 5.8E-01 | 7.0E-04 OK| | W-Mom-Bulk |23.57 | 2.4E-02 | 6.2E-01 | 2.5E-03 OK| | Mass-water |99.99 | 1.5E-03 | 5.6E-02 | 4.0E-02 ok| | Mass-air |99.99 | 9.6E-04 | 3.9E-02 | 12.5 2.2E-01 ok| +----------------------+------+---------+---------+------------------+ | K-TurbKE-Bulk | 0.38 | 1.1E-02 | 5.4E-01 | 10.7 5.1E-05 OK| | E-Diss.K-Bulk | 1.63 | 3.6E-02 | 9.9E-01 | 9.3 1.9E-03 OK| +----------------------+------+---------+---------+------------------+ ---------------------------------------------------------------------- | COUPLING/STAGGER ITERATION = 3 | ---------------------------------------------------------------------- | SOLVING : Mesh Displacement | ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | X-Disp |75.06 | 7.1E-02 | 6.7E-01 | 2.1E-08 OK| | Y-Disp |37.82 | 2.7E-02 | 2.4E-01 | 2.3E-08 OK| | Z-Disp |13.42 | 3.8E-02 | 3.8E-01 | 10.6 2.6E-08 OK| +----------------------+------+---------+---------+------------------+ | X-Disp | 0.04 | 2.9E-03 | 3.6E-02 | 3.3E-05 OK| | Y-Disp | 0.07 | 1.8E-03 | 1.9E-02 | 2.4E-06 OK| | Z-Disp | 0.04 | 1.6E-03 | 2.4E-02 | 10.6 3.8E-06 OK| +----------------------+------+---------+---------+------------------+ | X-Disp | 0.23 | 6.7E-04 | 7.1E-03 | 5.3E-05 OK| | Y-Disp | 0.31 | 5.4E-04 | 6.3E-03 | 1.7E-05 OK| | Z-Disp | 0.19 | 2.9E-04 | 2.5E-03 | 10.6 1.8E-05 OK| +----------------------+------+---------+---------+------------------+ | X-Disp | 0.15 | 9.8E-05 | 1.2E-03 | 4.0E-04 OK| | Y-Disp | 0.14 | 7.8E-05 | 1.1E-03 | 2.9E-05 OK| | Z-Disp | 0.16 | 4.8E-05 | 5.1E-04 | 10.6 1.4E-04 OK| +----------------------+------+---------+---------+------------------+ +--------------------------------------------------------------------+ | Mesh Statistics | +--------------------------------------------------------------------+ | Domain Name | Orthog. Angle | Exp. Factor | Aspect Ratio | +----------------------+---------------+--------------+--------------+ | | Minimum [deg] | Maximum | Maximum | +----------------------+---------------+--------------+--------------+ | Default Domain | 67.4 OK | 4 OK | 5 OK | +----------------------+---------------+--------------+--------------+ | | %! %ok %OK | %! %ok %OK | %! %ok %OK | +----------------------+---------------+--------------+--------------+ | Default Domain | 0 0 100 | 0 0 100 | 0 0 100 | +----------------------+---------------+--------------+--------------+ ---------------------------------------------------------------------- COEFFICIENT LOOP ITERATION = 7 CPU SECONDS = 9.274E+00 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom-Bulk | 1.72 | 3.6E-02 | 1.1E+00 | 2.2E-04 OK| | V-Mom-Bulk | 1.61 | 1.9E-02 | 7.8E-01 | 3.6E-04 OK| | W-Mom-Bulk | 1.86 | 4.4E-02 | 1.7E+00 | 1.6E-04 OK| | Mass-water | 3.65 | 5.5E-03 | 1.8E-01 | 5.4E-03 OK| | Mass-air | 5.34 | 5.1E-03 | 1.3E-01 | 16.3 1.1E-03 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE-Bulk | 6.64 | 7.4E-02 | 2.1E+00 | 10.3 8.6E-05 OK| | E-Diss.K-Bulk | 2.32 | 8.5E-02 | 2.7E+00 | 17.5 4.9E-06 OK| +----------------------+------+---------+---------+------------------+ ---------------------------------------------------------------------- COEFFICIENT LOOP ITERATION = 8 CPU SECONDS = 9.857E+00 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom-Bulk | 1.38 | 5.0E-02 | 1.9E+00 | 8.2E-04 OK| | V-Mom-Bulk | 2.08 | 4.0E-02 | 1.7E+00 | 7.1E-04 OK| | W-Mom-Bulk | 1.24 | 5.5E-02 | 2.8E+00 | 8.1E-04 OK| | Mass-water | 1.61 | 9.0E-03 | 2.5E-01 | 3.4E-03 OK| | Mass-air | 2.01 | 1.0E-02 | 2.9E-01 | 12.4 1.3E-03 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE-Bulk | 0.51 | 3.8E-02 | 5.0E-01 | 10.1 1.7E-03 OK| | E-Diss.K-Bulk | 0.45 | 3.8E-02 | 9.7E-01 | 17.5 3.8E-05 OK| +----------------------+------+---------+---------+------------------+ ---------------------------------------------------------------------- COEFFICIENT LOOP ITERATION = 9 CPU SECONDS = 1.042E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom-Bulk | 0.65 | 3.3E-02 | 6.1E-01 | 7.7E-04 OK| | V-Mom-Bulk | 0.97 | 3.9E-02 | 6.8E-01 | 8.1E-04 OK| | W-Mom-Bulk | 1.07 | 5.8E-02 | 2.5E+00 | 6.4E-04 OK| | Mass-water | 0.37 | 3.3E-03 | 6.7E-02 | 4.4E-03 OK| | Mass-air | 0.40 | 4.1E-03 | 8.7E-02 | 12.5 4.5E-04 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE-Bulk | 0.91 | 3.4E-02 | 6.0E-01 | 10.0 2.0E-04 OK| | E-Diss.K-Bulk | 1.02 | 3.9E-02 | 1.7E+00 | 17.4 4.1E-06 OK| +----------------------+------+---------+---------+------------------+ +--------------------------------------------------------------------+ | ERROR #001100279 has occurred in subroutine ErrAction. | | Message: | | CFX encountered the error: Read. Fatal error occurred when reque- | | sting Total Mesh Displacement for interface. | | | | | | | | | +--------------------------------------------------------------------+ +--------------------------------------------------------------------+ | ERROR #001100279 has occurred in subroutine ErrAction. | | Message: | | cplg_SendCommand failed to send the command: ERROR -- CFX encount- | | ered the error: Read. Fatal error occurred when requesting Total | | Mesh Displacement for interface. | | | | | | | +--------------------------------------------------------------------+ +--------------------------------------------------------------------+ | Writing crash recovery file | +--------------------------------------------------------------------+ +--------------------------------------------------------------------+ | ERROR #001100279 has occurred in subroutine ErrAction. | | Message: | | Stopped in routine cplg_SendCommand | | | | | | | | | | | +--------------------------------------------------------------------+ +--------------------------------------------------------------------+ | An error has occurred in cfx5solve: | | | | The ANSYS CFX solver exited with return code 1. No results file | | has been created. | +--------------------------------------------------------------------+ End of solution stage. +--------------------------------------------------------------------+ | An error has occurred in cfx5solve: | | | | ANSYS Solver terminated with return code 256 | +--------------------------------------------------------------------+ +--------------------------------------------------------------------+ | The results from this run of the ANSYS solver have been written to | | C:\Users\amir\Desktop\work\01_pending_tasks\dp0_CF X_Solution_1\Fl- | | uid Flow CFX_001.ansys | +--------------------------------------------------------------------+ +--------------------------------------------------------------------+ | Warning! | | | | The ANSYS CFX Solver has written a crash recovery file. This file | | has been saved as | | C:/Users/amir/Desktop/work/01_pending_tasks/dp0_CFX_Solution_1/Fl- | | uid Flow CFX_001.res.err and may be an aid to diagnosing the | | problem or restarting the run. More details should be available | | in the solver output section of the output file. | +--------------------------------------------------------------------+ +--------------------------------------------------------------------+ | The following user files have been saved in the directory | | C:/Users/amir/Desktop/work/01_pending_tasks/dp0_CFX_Solution_1/Fl- | | uid Flow CFX_001: | | | | mon | +--------------------------------------------------------------------+ This run of the ANSYS CFX Solver has finished. |
|
August 19, 2013, 04:53 |
|
#8 | |
Senior Member
Lance
Join Date: Mar 2009
Posts: 669
Rep Power: 22 |
Quote:
|
||
Tags |
cfx, solver error |
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
Remote cluster parallel solve without master, Ansys CFX 14.5 | aaguirre | CFX | 4 | January 27, 2015 10:15 |
Ansys CFX exited with return code 1. | dheelibun | CFX | 8 | May 7, 2014 08:21 |
how to map resultd from cfx to ansys? | ritesh | CFX | 2 | June 1, 2011 08:52 |
Fotran code in Ansys CFX | Abhishek Chitvar | CFX | 0 | December 20, 2008 12:19 |
FSI using CFX and ANSYS | Bi Chang | CFX | 2 | May 10, 2005 05:47 |