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Raport Simulare Cfd Hidrociclon

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Raport Simulare Cfd Hidrociclon
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This run of the CFX-14.0 Solver started at 16:39:49 on 14 June 2013 by user Puju on PUJU-PC (amd_opteron.sse2_winnt) using the command: "C:\Program Files\ANSYS Inc\v130\CFX\bin\ perllib\cfx5solve.pl" -batch -ccl runInput.ccl -fullname "HSSL_6 DES_001" Setting up CFX Solver run ... +------------------------------------------ --------------------------+ | | | CFX Command Language for Run | | | +------------------------------------------ --------------------------+ LIBRARY: CEL: EXPRESSIONS: AriaIntrare = 0.0001539 [m^2] ConcentratiaMasicaS1 = (DebMsolS1/ DebMamS1)*100 DebMamS1 = DebMapaS1 +DebMsolS1 DebMamS2 = DebMapaS2 +DebMsolS2 DebMamS3 = DebMapaS3 +DebMsolS3 DebMamS4 = DebMapaS4 +DebMsolS4 DebMamS5 = DebMapaS5 +DebMsolS5 DebMamS6 = DebMapaS6 +DebMsolS6 DebMamS7 = DebMapaS7 +DebMsolS7 DebMapaS1 = 0.11419 [kg s^-1] DebMapaS2 = 0.11407 [kg s^-1] DebMapaS3 = 0.11389 [kg s^-1] DebMapaS4 = 0.11364 [kg s^-1] DebMapaS5 = 0.11368 [kg s^-1] DebMapaS6 = 0.11352 [kg s^-1] DebMapaS7 = 0.12416 [kg s^-1] DebMsolS1 = 1.634e-3[kg s^-1] DebMsolS2 = 2.04e-3 [kg s^-1] DebMsolS3 = 2.445e-3 [kg s^-1] DebMsolS4 = 2.848e-3 [kg s^-1] DebMsolS5 = 3.009e-3 [kg s^-1] DebMsolS6 = 3.251e-3 [kg s^-1] DebMsolS7 = 3.64e-3 [kg s^-1] DensApa = 998 [kg m^-3] DensitateSolid = 2650 [kg m^-3] DensitateSuspensieS1 = 1.0069e3 [kg m^-3] DensitateSuspensieS2 = 1.0091e3 [kg m^-3] DensitateSuspensieS3 = 1.0112e3 [kg m^-3] DensitateSuspensieS4 = 1.0134e3 [kg m^-3] DensitateSuspensieS5 = 1.0143e3 [kg m^-3] DensitateSuspensieS6 = 1.0156e3 [kg m^-3] DensitateSuspensieS7 = 1.016e3 [kg m^-3] Dh = 0.014[m]
Transcript

This run of the CFX-14.0 Solver started at 16:39:49 on 14 June 2013 by user Puju on PUJU-PC (amd_opteron.sse2_winnt) using the command: "C:\Program Files\ANSYS Inc\v130\CFX\bin\perllib\cfx5solve.pl" -batch -ccl runInput.ccl -fullname "HSSL_6 DES_001" Setting up CFX Solver run ...

+--------------------------------------------------------------------+ | | | CFX Command Language for Run | | | +--------------------------------------------------------------------+

LIBRARY: CEL: EXPRESSIONS: AriaIntrare = 0.0001539 [m^2] ConcentratiaMasicaS1 = (DebMsolS1/ DebMamS1)*100 DebMamS1 = DebMapaS1 +DebMsolS1 DebMamS2 = DebMapaS2 +DebMsolS2 DebMamS3 = DebMapaS3 +DebMsolS3 DebMamS4 = DebMapaS4 +DebMsolS4 DebMamS5 = DebMapaS5 +DebMsolS5 DebMamS6 = DebMapaS6 +DebMsolS6 DebMamS7 = DebMapaS7 +DebMsolS7 DebMapaS1 = 0.11419 [kg s^-1] DebMapaS2 = 0.11407 [kg s^-1] DebMapaS3 = 0.11389 [kg s^-1] DebMapaS4 = 0.11364 [kg s^-1] DebMapaS5 = 0.11368 [kg s^-1] DebMapaS6 = 0.11352 [kg s^-1] DebMapaS7 = 0.12416 [kg s^-1] DebMsolS1 = 1.634e-3[kg s^-1] DebMsolS2 = 2.04e-3 [kg s^-1] DebMsolS3 = 2.445e-3 [kg s^-1] DebMsolS4 = 2.848e-3 [kg s^-1] DebMsolS5 = 3.009e-3 [kg s^-1] DebMsolS6 = 3.251e-3 [kg s^-1] DebMsolS7 = 3.64e-3 [kg s^-1] DensApa = 998 [kg m^-3] DensitateSolid = 2650 [kg m^-3] DensitateSuspensieS1 = 1.0069e3 [kg m^-3] DensitateSuspensieS2 = 1.0091e3 [kg m^-3] DensitateSuspensieS3 = 1.0112e3 [kg m^-3] DensitateSuspensieS4 = 1.0134e3 [kg m^-3] DensitateSuspensieS5 = 1.0143e3 [kg m^-3] DensitateSuspensieS6 = 1.0156e3 [kg m^-3] DensitateSuspensieS7 = 1.016e3 [kg m^-3] Dh = 0.014[m] DmedS1 = 80.47 [micron] DmedS2 = 87.18 [micron] DmedS3 = 93.36 [micron] DmedS4 = 97.63 [micron] DmedS5 = 104 [micron] DmedS6 = 106.2 [micron] DmedS7 = 107.41 [micron] FVapaS1 = 0.9946 FVapaS2 = 0.9933 FVapaS3 = 0.992 FVapaS4 = 0.9907 FVapaS5 = 0.9901 FVapaS6 = 0.9893 FVapaS7 = 0.9891 FVsolS1 = 1-FVapaS1 FVsolS2 = 1-FVapaS2 FVsolS3 = 1-FVapaS3 FVsolS4 = 1-FVapaS4 FVsolS5 = 1-FVapaS5 FVsolS6 = 1-FVapaS6 FVsolS7 = 1-FVapaS7 I = 0.037 PresIntrare = areaAve(p)@Intrare PresSupr = areaAve(p)@Suprascurgere VitSolid = DebMsolS1 /(AriaIntrare*DensitateSolid) VitSuspensie = DebMamS1 /(AriaIntrare * DensitateSuspensieS1) Volum = 0.000534889[m^3] deltaP = areaAve(p )@Intrare -areaAve(p)@Suprascurgere eps = (ka^1.5)/(0.3*Dh) ka = 1.5*(I^2)*(VitSuspensie^2) END END COORDINATE FRAME DEFINITIONS: COORDINATE FRAME: Coord 1 Centroid Type = Absolute Invert Normal Axis Direction = Off Location = F27.25 Option = Point and Normal Origin = 0.0688812 [m], 0.200441 [m], -2.97492e-007 [m] Point on Axis 3 = 0.0688812 [m], -0.799559 [m], -2.97492e-007 [m] Point on Plane 13 = 1 [m], 0 [m], 0 [m] Reference Coord Frame = Coord 0 END COORDINATE FRAME: Coord 2 Centroid Type = Absolute Invert Normal Axis Direction = Off Location = F41.25 Option = Point and Normal Origin = -0.0200005 [m], 0.1275 [m], 0.04 [m] Point on Axis 3 = -0.0200005 [m], 0.1275 [m], 1.04 [m] Point on Plane 13 = 1 [m], 0 [m], 0 [m] Reference Coord Frame = Coord 0 END END MATERIAL: Asphalt Material Group = CHT Solids,Particle Solids Option = Pure Substance Thermodynamic State = Solid PROPERTIES: Option = General Material EQUATION OF STATE: Density = 2650 [kg m^-3] Molar Mass = 1 [kg kmol^-1] Option = Value END SPECIFIC HEAT CAPACITY: Option = Value Specific Heat Capacity = 9.20E+02 [J kg^-1 K^-1] END REFERENCE STATE: Option = Specified Point Reference Specific Enthalpy = 0 [J/kg] Reference Specific Entropy = 0 [J/kg/K] Reference Temperature = 25 [C] END THERMAL CONDUCTIVITY: Option = Value Thermal Conductivity = 0.062 [W m^-1 K^-1] END END END MATERIAL: Nisip Material Group = User Materials List = Asphalt Option = Fixed Composition Mixture CHILD MATERIAL: Asphalt Mass Fraction = 1 Option = Mass Fraction END MIXTURE PROPERTIES: Option = Ideal Mixture DYNAMIC VISCOSITY: Dynamic Viscosity = 1 [Pa s] Option = Value 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: Option = None END INITIAL TIME: Option = Automatic with Value Time = 0 [s] END TIME DURATION: Option = Total Time Total Time = 2 [s] END TIME STEPS: Option = Timesteps Timesteps = 0.01 [s] END END DOMAIN: Ciclon Coord Frame = Coord 0 Domain Type = Fluid Location = Assembly BOUNDARY: Ciclon Default Boundary Type = WALL Location = \ F26.25,F28.25,F29.25,F30.25,F31.25,F32.25,F33.25,F34.25,F35.25,F36.25\ ,F37.25,F39.25,F40.25,F42.25,F43.25,F44.25,F45.25,F46.25,F47.25 BOUNDARY CONDITIONS: MASS AND MOMENTUM: Option = Fluid Dependent END WALL CONTACT MODEL: Option = Use Volume Fraction END WALL ROUGHNESS: Option = Smooth Wall END END FLUID: Nisip BOUNDARY CONDITIONS: MASS AND MOMENTUM: Option = No Slip Wall END END END FLUID: Water BOUNDARY CONDITIONS: MASS AND MOMENTUM: Option = No Slip Wall END END END END BOUNDARY: Intrare Boundary Type = INLET Location = F41.25 BOUNDARY CONDITIONS: FLOW REGIME: Option = Subsonic END MASS AND MOMENTUM: Option = Fluid Velocity END TURBULENCE: Option = Fluid Dependent END END FLUID: Nisip BOUNDARY CONDITIONS: FLOW DIRECTION: Option = Normal to Boundary Condition END SIZE GROUP: Group 1 Option = Value Size Fraction = 0.03 END SIZE GROUP: Group 2 Option = Value Size Fraction = 0.06 END SIZE GROUP: Group 3 Option = Value Size Fraction = 0.1 END SIZE GROUP: Group 4 Option = Value Size Fraction = 0.15 END SIZE GROUP: Group 5 Option = Value Size Fraction = 0.28 END SIZE GROUP: Group 6 Option = Value Size Fraction = 0.16 END SIZE GROUP: Group 7 Option = Value Size Fraction = 0.22 END VELOCITY: Mass Flow Rate = DebMsolS1 Option = Mass Flow Rate END VOLUME FRACTION: Option = Value Volume Fraction = FVsolS1 END END END FLUID: Water BOUNDARY CONDITIONS: FLOW DIRECTION: Option = Normal to Boundary Condition END TURBULENCE: Epsilon = eps Option = k and Epsilon k = ka END VELOCITY: Mass Flow Rate = DebMapaS1 Option = Mass Flow Rate END VOLUME FRACTION: Option = Value Volume Fraction = FVapaS1 END END END END BOUNDARY: Scurgere Boundary Type = OUTLET Location = F38.25 BOUNDARY CONDITIONS: FLOW REGIME: Option = Subsonic END MASS AND MOMENTUM: Option = Average Static Pressure Pressure Profile Blend = 0.05 Relative Pressure = 0 [Pa] END PRESSURE AVERAGING: Option = Average Over Whole Outlet END END END BOUNDARY: Suprascurgere Boundary Type = OUTLET Location = F27.25 BOUNDARY CONDITIONS: FLOW REGIME: Option = Subsonic END MASS AND MOMENTUM: Option = Average Static Pressure Pressure Profile Blend = 0.05 Relative Pressure = 0 [Pa] END PRESSURE AVERAGING: Option = Average Over Whole Outlet END END END DOMAIN MODELS: BUOYANCY MODEL: Buoyancy Reference Density = 998 [kg m^-3] Gravity X Component = 0 [m s^-2] Gravity Y Component = -9.81 [m s^-2] Gravity Z Component = 0 [m s^-2] Option = Buoyant BUOYANCY REFERENCE LOCATION: Option = Automatic END END DOMAIN MOTION: Option = Stationary END MESH DEFORMATION: Option = None END REFERENCE PRESSURE: Reference Pressure = 1 [atm] END END FLUID DEFINITION: Nisip Material = Nisip Option = Material Library MORPHOLOGY: Option = Polydispersed 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: Nisip FLUID BUOYANCY MODEL: Option = Density Difference END TURBULENCE MODEL: Option = Dispersed Phase Zero Equation END END FLUID: Water FLUID BUOYANCY MODEL: Option = Density Difference END TURBULENCE MODEL: Option = DES SST BUOYANCY TURBULENCE: Option = None END END TURBULENT WALL FUNCTIONS: Option = Automatic END END HEAT TRANSFER MODEL: Homogeneous Model = False Option = None END THERMAL RADIATION MODEL: Option = None END TURBULENCE MODEL: Homogeneous Model = False Option = Fluid Dependent END END FLUID PAIR: Nisip | Water INTERPHASE TRANSFER MODEL: Option = Particle Model END MASS TRANSFER: Option = None END MOMENTUM TRANSFER: DRAG FORCE: Option = Schiller Naumann END LIFT FORCE: Lift Coefficient = 0.5 Option = Lift Coefficient END TURBULENT DISPERSION FORCE: Option = None END VIRTUAL MASS FORCE: Option = None END WALL LUBRICATION FORCE: Option = None END END TURBULENCE TRANSFER: ENHANCED TURBULENCE PRODUCTION MODEL: Option = None END END END INITIALISATION: Option = Automatic FLUID: Nisip INITIAL CONDITIONS: Velocity Type = Cylindrical CYLINDRICAL VELOCITY COMPONENTS: Option = Automatic with Value Velocity Axial Component = 0 [m s^-1] Velocity Theta Component = 0 [m s^-1] Velocity r Component = 0 [m s^-1] AXIS DEFINITION: Option = Coordinate Axis Rotation Axis = Coord 0.2 END END SIZE GROUP: Group 1 Option = Automatic with Value Size Fraction = 0.03 END SIZE GROUP: Group 2 Option = Automatic with Value Size Fraction = 0.06 END SIZE GROUP: Group 3 Option = Automatic with Value Size Fraction = 0.1 END SIZE GROUP: Group 4 Option = Automatic with Value Size Fraction = 0.15 END SIZE GROUP: Group 5 Option = Automatic with Value Size Fraction = 0.28 END SIZE GROUP: Group 6 Option = Automatic with Value Size Fraction = 0.16 END SIZE GROUP: Group 7 Option = Automatic with Value Size Fraction = 0.22 END VOLUME FRACTION: Option = Automatic with Value Volume Fraction = FVsolS1 END END END FLUID: Water INITIAL CONDITIONS: Velocity Type = Cylindrical CYLINDRICAL VELOCITY COMPONENTS: Option = Automatic with Value Velocity Axial Component = 0 [m s^-1] Velocity Theta Component = 0 [m s^-1] Velocity r Component = 0 [m s^-1] AXIS DEFINITION: Option = Coordinate Axis Rotation Axis = Coord 0.2 END END TURBULENCE INITIAL CONDITIONS: Option = k and Epsilon EPSILON: Epsilon = eps Option = Automatic with Value END K: Option = Automatic with Value k = ka END END VOLUME FRACTION: Option = Automatic with Value Volume Fraction = FVapaS1 END END END INITIAL CONDITIONS: STATIC PRESSURE: Option = Automatic with Value Relative Pressure = 0 [Pa] END END END MULTIPHASE MODELS: Homogeneous Model = False FREE SURFACE MODEL: Option = None END POLYDISPERSED FLUID: Musig Fluid 1 Option = Homogeneous MUSIG Polydispersed Fluid = Nisip BREAKUP MODEL: Option = None END COALESCENCE MODEL: Option = None END SIZE GROUP DISTRIBUTION: Number of Size Groups = 7 Option = User Defined SIZE GROUP: Group 1 Option = Definition Polydispersed Fluid = Nisip Size Group Diameter = 12 [micron] END SIZE GROUP: Group 2 Option = Definition Polydispersed Fluid = Nisip Size Group Diameter = 17 [micron] END SIZE GROUP: Group 3 Option = Definition Polydispersed Fluid = Nisip Size Group Diameter = 58 [micron] END SIZE GROUP: Group 4 Option = Definition Polydispersed Fluid = Nisip Size Group Diameter = 75 [micron] END SIZE GROUP: Group 5 Option = Definition Polydispersed Fluid = Nisip Size Group Diameter = 110 [micron] END SIZE GROUP: Group 6 Option = Definition Polydispersed Fluid = Nisip Size Group Diameter = 121 [micron] END SIZE GROUP: Group 7 Option = Definition Polydispersed Fluid = Nisip Size Group Diameter = 132 [micron] END END END END END OUTPUT CONTROL: MONITOR OBJECTS: Monitor Coefficient Loop Convergence = False MONITOR BALANCES: Option = Full END MONITOR FORCES: Option = Full END MONITOR PARTICLES: Option = Full END MONITOR POINT: Monitor Point 1 Cartesian Coordinates = 0.0[m],0.0[m],0.0[m] Coord Frame = Coord 0 Option = Cartesian Coordinates Output Variables List = Vorticity END MONITOR POINT: Monitor Point 2 Cartesian Coordinates = 0.0[m],0.0[m],0.0[m] Coord Frame = Coord 1 Option = Cartesian Coordinates Output Variables List = Vorticity END MONITOR POINT: Monitor Point 3 Cartesian Coordinates = 0.0[m],0.0[m],0.0[m] Coord Frame = Coord 2 Option = Cartesian Coordinates Output Variables List = Vorticity END MONITOR RESIDUALS: Option = Full END MONITOR TOTALS: Option = Full END END RESULTS: File Compression Level = Default Option = Standard END TRANSIENT RESULTS: Transient Results 1 File Compression Level = Default Option = Standard OUTPUT FREQUENCY: Option = Time Interval Time Interval = 2 [s] END END END SOLVER CONTROL: Turbulence Numerics = First Order ADVECTION SCHEME: Option = High Resolution END CONVERGENCE CONTROL: Maximum Number of Coefficient Loops = 1 Minimum Number of Coefficient Loops = 1 Timescale Control = Coefficient Loops END CONVERGENCE CRITERIA: Conservation Target = 0.01 Residual Target = 1.E-4 Residual Type = RMS END TRANSIENT SCHEME: Option = Second Order Backward Euler TIMESTEP INITIALISATION: Option = Automatic END END END EXPERT PARAMETERS: include pref in forces = t transient initialisation override = t END END COMMAND FILE: Version = 13.0 Results Version = 13.0 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 PARALLEL HOST LIBRARY: HOST DEFINITION: pujupc Remote Host Name = PUJU-PC Host Architecture String = winnt 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 = HSSL_6 DES.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 END END END

+--------------------------------------------------------------------+ | | | Solver | | | +--------------------------------------------------------------------+

+--------------------------------------------------------------------+ | | | ANSYS CFX Solver 13.0 | | | | Version 2010.10.01-23.02 Sat Oct 2 02:26:59 GMTDT 2010 | | | | Executable Attributes | | | | single-int32-32bit-novc8-noifort-novc6-optimised-supfort-noprof-nos| | | | Copyright 2010 ANSYS Inc. | +--------------------------------------------------------------------+

+--------------------------------------------------------------------+ | Job Information | +--------------------------------------------------------------------+

Run mode: serial run

Host computer: PUJU-PC (PID:5508) Job started: Mon Mar 14 16:39:57 2011

+--------------------------------------------------------------------+ | Memory Allocated for Run (Actual usage may be less) | +--------------------------------------------------------------------+

Data Type Kwords Words/Node Words/Elem Kbytes Bytes/Node Real 30746.4 1575.52 319.15 120103.0 6302.10 Integer 4376.5 224.26 45.43 17095.6 897.05 Character 3739.7 191.63 38.82 3652.1 191.63 Logical 80.0 4.10 0.83 312.5 16.40 Double 602.5 30.88 6.25 4707.3 247.00

+--------------------------------------------------------------------+ | MUSIG Size Group Information | +--------------------------------------------------------------------+

Domain name : Ciclon

MUSIG fluid : Musig Fluid 1

Group Polydispersed Fluid Diameter Mass Group 1 Nisip 1.2000E-05 2.3977E-12 Group 2 Nisip 1.7000E-05 6.8170E-12 Group 3 Nisip 5.8000E-05 2.7073E-10 Group 4 Nisip 7.5000E-05 5.8537E-10 Group 5 Nisip 1.1000E-04 1.8468E-09 Group 6 Nisip 1.2100E-04 2.4581E-09 Group 7 Nisip 1.3200E-04 3.1913E-09

+--------------------------------------------------------------------+ | Mesh Statistics | +--------------------------------------------------------------------+ | Domain Name | Orthog. Angle | Exp. Factor | Aspect Ratio | +----------------------+---------------+--------------+--------------+ | | Minimum [deg] | Maximum | Maximum | +----------------------+---------------+--------------+--------------+ | Ciclon | 44.3 ok | 46 ! | 14 OK | +----------------------+---------------+--------------+--------------+ | | %! %ok %OK | %! %ok %OK | %! %ok %OK | +----------------------+---------------+--------------+--------------+ | Ciclon | 0


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