|
[Sponsors] |
June 18, 2010, 17:07 |
Fatal error
|
#1 |
Member
Join Date: Jun 2010
Posts: 77
Rep Power: 16 |
I got a strange error in CFX, i have copied here the output file (bold characters). Could anyone help? Thanks!
This run of the CFX-12.1 Solver started at 23:04:11 on 18 Jun 2010 by user Theo on THEO-PC (intel_xeon64.sse2_winnt) using the command: "C:\Program Files\ANSYS Inc\v121\CFX\bin\perllib\cfx5solve.pl" -batch -ccl C:\Users\Theo\AppData\Local\Temp\unsaved_project_7 860_Working\dp0\CFX\CFX\Work1\runInput.ccl -file-comms C:\Users\Theo\AppData\Local\Temp\unsaved_project_7 860_Working\dp0\CFX\CFX\Work1\runInfo.ccl Setting up CFX Solver run ... +--------------------------------------------------------------------+ | | | CFX Command Language for Run | | | +--------------------------------------------------------------------+ LIBRARY: 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 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 = Steady State EXTERNAL SOLVER COUPLING: Option = None END END DOMAIN: Default Domain Coord Frame = Coord 0 Domain Type = Fluid Location = B1661, B1662, B311 BOUNDARY: Default Domain Default Boundary Type = WALL Location = \ F1450.311,F1451.311,F1452.311,F1453.311,F1454.311, F1455.311,F1456.311\ ,F1457.311,F1458.311,F1459.311,F1460.311,F1461.311 ,F1462.311,F1463.31\ 1,F1464.311,F1465.311,F1466.311,F1467.311,F1468.31 1,F1469.311,F1470.3\ 11,F1471.311,F1472.311,F1473.311,F1474.311,F1475.3 11,F1476.311,F1477.\ 311,F1478.311,F1479.311,F1480.311,F1481.311,F1482. 311,F1483.311,F1484\ .311,F1485.311,F1486.311,F1487.311,F1488.311,F1489 .311,F1490.311,F149\ 1.311,F1492.311,F1493.311,F1494.311,F1495.311,F149 6.311,F1497.311,F14\ 98.311,F1499.311,F1500.311,F1501.311,F1502.311,F15 03.311,F1504.311,F1\ 505.311,F1506.311,F1507.311,F1508.311,F1509.311,F1 510.311,F1511.311,F\ 1512.311,F1513.311,F1514.311,F1515.311,F1516.311,F 1517.311,F1518.311,\ F1519.311,F1520.311,F1521.311,F1522.311,F1523.311, F1524.311,F1525.311\ ,F1526.311,F1527.311,F1528.311,F1529.311,F1530.311 ,F1531.311,F1532.31\ 1,F1533.311,F1534.311,F1535.311,F1536.311,F1537.31 1,F1538.311,F1539.3\ 11,F1540.311,F1541.311,F1542.311,F1543.311,F1544.3 11,F1545.311,F1546.\ 311,F1547.311,F1548.311,F1549.311,F1550.311,F1551. 311,F1552.311,F1553\ .311,F1554.311,F1555.311,F1556.311,F1557.311,F1558 .311,F1559.311,F156\ 0.311,F1561.311,F1562.311,F1563.311,F1564.311,F156 5.311,F1566.311,F15\ 67.311,F1568.311,F1569.311,F1570.311,F1571.311,F15 72.311,F1573.311,F1\ 574.311,F1575.311,F1576.311,F1577.311,F1578.311,F1 579.311,F1580.311,F\ 1581.1661,F1582.1661,F1585.1661,F1586.1661,F1587.1 661,F1588.1661,F158\ 9.1662,F1590.1662,F1591.1662,F1592.1662,F1595.1662 ,F1596.1662,F253.31\ 1,F254.311,F255.311,F256.311,F258.311,F259.311,F26 0.311,F261.311,F262\ .311,F263.311,F264.311,F265.311,F266.311,F267.311, F268.311,F269.311,F\ 270.311,F271.311,F272.311,F273.311,F274.311,F275.3 11,F276.311,F277.31\ 1,F278.311,F279.311,F280.311,F282.311,F283.311,F28 4.311,F285.311,F286\ .311,F287.311,F288.311,F289.311,F290.311,F291.311, F292.311,F293.311,F\ 294.311,F295.311,F296.311,F297.311,F298.311,F299.3 11,F300.311,F301.31\ 1,F302.311,F303.311,F304.311,F305.311,F306.311 BOUNDARY CONDITIONS: MASS AND MOMENTUM: Option = No Slip Wall END WALL ROUGHNESS: Option = Smooth Wall END END END BOUNDARY: Inlet Boundary Type = INLET Location = F257.311 BOUNDARY CONDITIONS: FLOW REGIME: Option = Subsonic END MASS AND MOMENTUM: Normal Speed = 28 [m s^-1] Option = Normal Speed END TURBULENCE: Option = Medium Intensity and Eddy Viscosity Ratio END END END BOUNDARY: Outlet Boundary Type = OUTLET Location = F252.311 BOUNDARY CONDITIONS: FLOW REGIME: Option = Subsonic END MASS AND MOMENTUM: Option = Average Static Pressure Pressure Profile Blend = 0.05 Relative Pressure = 2 [Pa] END PRESSURE AVERAGING: Option = Average Over Whole Outlet END END END DOMAIN MODELS: BUOYANCY MODEL: Option = Non Buoyant END DOMAIN MOTION: Option = Stationary END MESH DEFORMATION: Option = None END REFERENCE PRESSURE: Reference Pressure = 1 [atm] END END FLUID DEFINITION: Fluid 1 Material = Air at 25 C Option = Material Library MORPHOLOGY: Option = Continuous Fluid END END FLUID MODELS: COMBUSTION MODEL: Option = None END HEAT TRANSFER MODEL: Fluid Temperature = 25 [C] Option = Isothermal END THERMAL RADIATION MODEL: Option = None END TURBULENCE MODEL: Option = k epsilon END TURBULENT WALL FUNCTIONS: Option = Scalable END END END OUTPUT CONTROL: RESULTS: File Compression Level = Default Option = Standard END END SOLVER CONTROL: Turbulence Numerics = First Order ADVECTION SCHEME: Option = High Resolution END CONVERGENCE CONTROL: Length Scale Option = Conservative Maximum Number of Iterations = 100 Minimum Number of Iterations = 1 Timescale Control = Auto Timescale Timescale Factor = 1.0 END CONVERGENCE CRITERIA: Residual Target = 1.E-4 Residual Type = RMS END DYNAMIC MODEL CONTROL: Global Dynamic Model Control = On END END END COMMAND FILE: Version = 12.1 Results Version = 12.1 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 PARALLEL HOST LIBRARY: HOST DEFINITION: theopc Remote Host Name = THEO-PC Host Architecture String = winnt-amd64 Installation Root = C:\Program Files\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 = \ C:\Users\Theo\AppData\Local\Temp\unsaved_project_7 860_Working\dp0\CFX\ \CFX\Work1\Fluid Flow.def INITIAL VALUES SPECIFICATION: INITIAL VALUES CONTROL: Use Mesh From = Solver Input File Continue History From = Workbench Initial Values END INITIAL VALUES: Workbench Initial Values Option = Results File File Name = \ C:\Users\Theo\AppData\Local\Temp\unsaved_project_7 860_Working\dp0\ \CFX\CFX\Work1\Fluid Flow_001.res END END 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 END END END +--------------------------------------------------------------------+ | | | Interpolation of Initial Values | | | +--------------------------------------------------------------------+ +--------------------------------------------------------------------+ | | | ANSYS CFX Interpolator 12.1 | | | | Version 2009.10.14-23.08 Thu Oct 15 00:45:24 GMTDT 2009 | | | | Executable Attributes | | | | single-int32-64bit-novc8-noifort-novc6-optimised-supfort-noprof-nos| | | | Copyright 2009 ANSYS Inc. | +--------------------------------------------------------------------+ +--------------------------------------------------------------------+ | Job Information | +--------------------------------------------------------------------+ Run mode: serial run Host computer: THEO-PC Job started: Fri Jun 18 23:04:12 2010 +--------------------------------------------------------------------+ | Memory Allocated for Run (Actual usage may be less) | +--------------------------------------------------------------------+ Data Type Kwords Words/Node Words/Elem Kbytes Bytes/Node Real 65212.1 69.17 13.09 254734.7 276.68 Integer 89353.8 94.78 17.94 349038.3 379.10 Character 200.0 0.21 0.04 195.3 0.21 Logical 10.0 0.01 0.00 39.1 0.04 Double 300.0 0.32 0.06 2343.8 2.55 ================================================== ==================== Interpolating Onto Domain "Default Domain" ================================================== ==================== Total Number of Nodes in the Target Domain = 942790 Bounding Box Volume of the Target Mesh = 2.52303E+02 Checking all source domains from the source file: Target mesh is the same as domain "Default Domain". Start direct copying of variables from domain "Default Domain". +--------------------------------------------------------------------+ | Variable Range Information | +--------------------------------------------------------------------+ +--------------------------------------------------------------------+ | Variable Name | min | max | +--------------------------------------------------------------------+ | Thermal Conductivity | 2.61E-02 | 2.61E-02 | | Courant Number | 0.00E+00 | 0.00E+00 | | Density | 1.18E+00 | 1.18E+00 | | Isolated Volumes | 1.00E+00 | 3.00E+00 | | Static Entropy | 0.00E+00 | 0.00E+00 | | Pressure | 0.00E+00 | 0.00E+00 | | Specific Heat Capacity at Constant Pressure| 1.00E+03 | 1.00E+03 | | Turbulence Eddy Dissipation | 5.03E+03 | 5.03E+03 | | Temperature | 2.98E+02 | 2.98E+02 | | Turbulence Kinetic Energy | 2.94E+00 | 2.94E+00 | | Velocity | 2.80E+01 | 2.80E+01 | | Dynamic Viscosity | 1.83E-05 | 1.83E-05 | | Eddy Viscosity | 1.83E-04 | 1.83E-04 | Details of error:- Details of error:- ---------------- ---------------- Error detected by routine MAKDAT Error detected by routine MAKDAT Illegal data area length CDANAM = NCOMPT CDTYPE = INTR ISIZE = 0 Illegal data area length CDANAM = NCOMPT CDTYPE = INTR ISIZE = 0 CRESLT = SIZE CRESLT = SIZE Current Directory : /INTERP/SOLUTION/DST/VX Current Directory : /INTERP/SOLUTION/DST/VX +================================================= ===================+ | ****** PROBLEM REPORT ****** | |--------------------------------------------------------------------| | Subsystem: Input | | Subroutine name: ErrAction | | Severity level: Fatal Error | | Error message number: 001100279 | |--------------------------------------------------------------------| | Message: | | | | Stopped in routine MEMERR | | | | | | | | | | | +================================================= ===================+ +--------------------------------------------------------------------+ | An error has occurred in cfx5solve: | | | | Error interpolating results onto the new mesh: C:\Program | | Files\ANSYS Inc\v121\CFX\bin\winnt-amd64\solver-hpmpi.exe exited | | with return code 1. | +--------------------------------------------------------------------+ +--------------------------------------------------------------------+ | The following user files have been saved in the directory | | C:\Users\Theo\AppData\Local\Temp\unsaved_project_7 860_Working\dp0- | | \CFX\CFX\Work1\Fluid Flow_006: | | | | job | +--------------------------------------------------------------------+ This run of the ANSYS CFX Solver has finished. |
|
June 20, 2010, 07:33 |
|
#2 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,854
Rep Power: 144 |
I am just guessing but I think the interpolation routine to get your initial guess ran out of memory. Best do the interpolation on a machine with more memory, or at least make sure nothing else is running which gobbles up memory. There are also some memory options on the interpolator, these might help - see the documentation for these.
|
|
May 26, 2014, 02:04 |
|
#3 |
New Member
george
Join Date: May 2014
Posts: 3
Rep Power: 12 |
I am getting a similar kind of error...but running it on machine with higher memory does not solve it....where to find the interpolater settings??
|
|
May 26, 2014, 09:53 |
|
#4 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,854
Rep Power: 144 |
Have a look in the documentation. There is a command line utility which can do interpolation which has lots of options documented.
|
|
September 13, 2016, 06:50 |
|
#5 |
New Member
No Real Name
Join Date: Sep 2016
Posts: 4
Rep Power: 10 |
Hello Glenn,
I see that you have responded to this problem as a problem with "memory" quite a few times. I find that quite strange because it seems completely ridiculous. The solver states it very specifically if it has an issue with the memory and is not ambiguously going to point you to another direction in such a way. The problem is with the mesh. Given the initial values, it is not possible for the solver, for some reason, to interpolate for other locations. It is therefore wise to take a look at the mesh and not waste any time with the memory. There is nothing, absolutely nothing, wrong with the memory here. Have a nice day. |
|
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
CGNS Compiling | Diego | Main CFD Forum | 17 | December 21, 2014 02:40 |
UDF: DEFINE_CG_MOTION for vertical jump motion of an electrode! | alban | Fluent UDF and Scheme Programming | 2 | June 8, 2010 19:54 |
[Netgen] Installation of Netgen in SuSE Linux 92 | edvardsenpriv | OpenFOAM Meshing & Mesh Conversion | 23 | January 16, 2009 07:12 |
Problem with compile the setParabolicInlet | ivanyao | OpenFOAM Running, Solving & CFD | 6 | September 5, 2008 21:50 |
a question of open ".cas" and ".dat" files | fanzhong Meng | FLUENT | 4 | May 15, 2006 12:40 |