coffee husk outfiles.txt - notepad

coffee husk outfiles.txt This run of the CFX-12.1 Solver started at 16:57:24 on 20 Jun 2012 by user User on USER-E0D9062D4B (intel_xeon64.sse2_winnt) using the command: "C:\Program Files\ANSYS Inc\v121\CFX\bin\perllib\cfx5solve.pl" -batch -ccl "C:\Documents and Settings\User\Local Settings\Temp\coffee husk gasifier_2396_Working\dp0\CFX\CFX\Work1\runInput.ccl" -file-comms "C:\Documents and Settings\User\Local Settings\Temp\coffee husk gasifier_2396_Working\dp0\CFX\CFX\Work1\runInfo.ccl" Setting up CFX Solver run ...

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

LIBRARY: MATERIAL: Ash Material Group = Particle Solids Option = Pure Substance Thermodynamic State = Solid PROPERTIES: Option = General Material EQUATION OF STATE: Density = 1000 [kg m^-3] Molar Mass = 12 [kg kmol^-1] Option = Value END SPECIFIC HEAT CAPACITY: Option = Value Specific Heat Capacity = 800 [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 END END MATERIAL: CO2 Material Description = Carbon Dioxide CO2 Material Group = Gas Phase Combustion Option = Pure Substance Thermodynamic State = Gas PROPERTIES: Option = General Material EQUATION OF STATE: Molar Mass = 44.01 [kg kmol^-1] Option = Ideal Gas END SPECIFIC HEAT CAPACITY: Option = NASA Format LOWER INTERVAL COEFFICIENTS: NASA a1 = 0.02275725E+02 [] NASA a2 = 0.09922072E-01 [K^-1] NASA a3 = -0.01040911E-03 [K^-2] NASA a4 = 0.06866687E-07 [K^-3]

coffee husk outfiles.txt NASA a5 = -0.02117280E-10 [K^-4] NASA a6 = -0.04837314E+06 [K] NASA a7 = 0.01018849E+03 [] END TEMPERATURE LIMITS: Lower Temperature = 300 [K] Midpoint Temperature = 1000 [K] Upper Temperature = 5000 [K] END UPPER INTERVAL COEFFICIENTS: NASA a1 = 0.04453623E+02 [] NASA a2 = 0.03140169E-01 [K^-1] NASA a3 = -0.01278411E-04 [K^-2] NASA a4 = 0.02393997E-08 [K^-3] NASA a5 = -0.01669033E-12 [K^-4] NASA a6 = -0.04896696E+06 [K] NASA a7 = -0.09553959E+01 [] END END REFERENCE STATE: Option = NASA Format Reference Pressure = 1 [atm] Reference Temperature = 25 [C] END DYNAMIC VISCOSITY: Dynamic Viscosity = 14.9E-06 [kg m^-1 s^-1] Option = Value END THERMAL CONDUCTIVITY: Option = Value Thermal Conductivity = 145E-04 [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 END END MATERIAL: Char Material Group = Particle Solids Option = Pure Substance Thermodynamic State = Solid PROPERTIES: Option = General Material EQUATION OF STATE: Density = 2000 [kg m^-3] Molar Mass = 12 [kg kmol^-1] Option = Value END SPECIFIC HEAT CAPACITY: Option = Value Specific Heat Capacity = 1600 [J kg^-1 K^-1] END REFERENCE STATE: Option = Specified Point

coffee husk outfiles.txt Reference Specific Enthalpy = 0 [J/kg] Reference Specific Entropy = 0 [J/kg/K] Reference Temperature = 25 [C] END END END MATERIAL: Fuel Gas Material Description = Generalized Fuel Gas Molecule (Properties taken \ from Methane CH4) Material Group = Gas Phase Combustion Option = Pure Substance Thermodynamic State = Gas PROPERTIES: Option = General Material EQUATION OF STATE: Molar Mass = 16 [kg kmol^-1] Option = Ideal Gas END SPECIFIC HEAT CAPACITY: Option = Value Specific Heat Capacity = 2210 [J kg^-1 K^-1] Specific Heat Type = Constant Pressure END REFERENCE STATE: Option = Specified Point Reference Pressure = 1 [atm] Reference Specific Enthalpy = -4.7232670E+06 [J/kg] Reference Specific Entropy = 1.1405054E+04 [J/kg/K] Reference Temperature = 25 [C] END DYNAMIC VISCOSITY: Dynamic Viscosity = 11.1E-06 [kg m^-1 s^-1] Option = Value END THERMAL CONDUCTIVITY: Option = Value Thermal Conductivity = 343E-04 [W m^-1 K^-1] END ABSORPTION COEFFICIENT: Absorption Coefficient = 1 [m^-1] Option = Value END SCATTERING COEFFICIENT: Option = Value Scattering Coefficient = 0 [m^-1] END REFRACTIVE INDEX: Option = Value Refractive Index = 1 [m m^-1] END END END MATERIAL: Gas Mixture Additional Materials List = N2 Material Description = Gas Mixture without Pollutants Material Group = Gas Phase Combustion Option = Reacting Mixture Reactions List = Fuel Gas Oxygen Thermodynamic State = Gas END MATERIAL: H2O Material Description = Water Vapour Material Group = Gas Phase Combustion, Interphase Mass Transfer, Water \

coffee husk outfiles.txt Data Option = Pure Substance Thermodynamic State = Gas PROPERTIES: Option = General Material EQUATION OF STATE: Molar Mass = 18.02 [kg kmol^-1] Option = Ideal Gas END SPECIFIC HEAT CAPACITY: Option = NASA Format LOWER INTERVAL COEFFICIENTS: NASA a1 = 0.03386842E+02 [] NASA a2 = 0.03474982E-01 [K^-1] NASA a3 = -0.06354696E-04 [K^-2] NASA a4 = 0.06968581E-07 [K^-3] NASA a5 = -0.02506588E-10 [K^-4] NASA a6 = -0.03020811E+06 [K] NASA a7 = 0.02590233E+02 [] END TEMPERATURE LIMITS: Lower Temperature = 300 [K] Midpoint Temperature = 1000 [K] Upper Temperature = 5000 [K] END UPPER INTERVAL COEFFICIENTS: NASA a1 = 0.02672146E+02 [] NASA a2 = 0.03056293E-01 [K^-1] NASA a3 = -0.08730260E-05 [K^-2] NASA a4 = 0.01200996E-08 [K^-3] NASA a5 = -0.06391618E-13 [K^-4] NASA a6 = -0.02989921E+06 [K] NASA a7 = 0.06862817E+02 [] END END REFERENCE STATE: Option = NASA Format Reference Pressure = 1 [atm] Reference Temperature = 25 [C] END DYNAMIC VISCOSITY: Dynamic Viscosity = 9.4E-06 [kg m^-1 s^-1] Option = Value END THERMAL CONDUCTIVITY: Option = Value Thermal Conductivity = 193E-04 [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 END END MATERIAL: HC Fuel

coffee husk outfiles.txt Material Description = Hydrocarbon Fuel Mixture Material Material Group = Particle Solids Option = Hydrocarbon Fuel Thermodynamic State = Solid MATERIAL ANALYSIS: HEATING VALUE: Heating Value = 17.945 [MJ/kg] Option = Higher Heating Value Reference Pressure = 1 [atm] Reference Temperature = 25 [C] MOISTURE LATENT HEAT: Latent Heat = 2.4423 [MJ/kg] Option = Value Reference Pressure = 1 [atm] Reference Temperature = 25 [C] END END PROXIMATE ANALYSIS: Ash Fraction = 0.0068 Fixed Carbon Fraction = 0.155 Moisture Fraction = 0.0722 Option = As Received Volatiles Fraction = 0.766 END ULTIMATE ANALYSIS: Carbon Fraction = 0.4651 Chlorine Fraction = 0.0000 Hydrogen Fraction = 0.0677 Nitrogen Fraction = 0.0043 Option = Dry Ash Free Oxygen Fraction = 0.4620 Sulphur Fraction = 0.0009 END VOLATILES RELEASE: Enhancement of Yield = 1.25 VOLATILES MOLAR MASS: Option = Automatic END END END MIXTURE MATERIALS: Binary Mixture Material = HC Fuel Gas Binary Mixture GAS MIXTURE: Carbon Dioxide Material = CO2 Mixture Material = Gas Mixture Nitrogen Material = N2 Option = Mixture Oxygen Material = O2 Volatiles Fuel Material = Fuel Gas Water Vapour Material = H2O END PARTICLE MIXTURE: Ash Material = Ash Char Material = Char Option = Ash Char and Raw Combustible Raw Combustible Material = Raw Combustible END END END MATERIAL: HC Fuel Gas Binary Mixture Binary Material1 = Raw Combustible Binary Material2 = Fuel Gas Material Group = Gas Phase Combustion, Particle Solids

coffee husk outfiles.txt Option = Homogeneous Binary Mixture SATURATION PROPERTIES: Option = General PRESSURE: Antoine Enthalpic Coefficient B = 8418.25 [K] Antoine Pressure Scale = 1 [Pa] Antoine Reference State Constant A = 30.2212 Antoine Temperature Offset C = 0 [K] Option = Antoine Equation END TEMPERATURE: Option = Automatic END END END MATERIAL: N2 Material Description = Nitrogen N2 Material Group = Gas Phase Combustion Option = Pure Substance Thermodynamic State = Gas PROPERTIES: Option = General Material EQUATION OF STATE: Molar Mass = 28.01 [kg kmol^-1] Option = Ideal Gas END SPECIFIC HEAT CAPACITY: Option = NASA Format LOWER INTERVAL COEFFICIENTS: NASA a1 = 0.03298677E+02 [] NASA a2 = 0.01408240E-01 [K^-1] NASA a3 = -0.03963222E-04 [K^-2] NASA a4 = 0.05641515E-07 [K^-3] NASA a5 = -0.02444855E-10 [K^-4] NASA a6 = -0.01020900E+05 [K] NASA a7 = 0.03950372E+02 [] END TEMPERATURE LIMITS: Lower Temperature = 300 [K] Midpoint Temperature = 1000 [K] Upper Temperature = 5000 [K] END UPPER INTERVAL COEFFICIENTS: NASA a1 = 0.02926640E+02 [] NASA a2 = 0.01487977E-01 [K^-1] NASA a3 = -0.05684761E-05 [K^-2] NASA a4 = 0.01009704E-08 [K^-3] NASA a5 = -0.06753351E-13 [K^-4] NASA a6 = -0.09227977E+04 [K] NASA a7 = 0.05980528E+02 [] END END REFERENCE STATE: Option = NASA Format Reference Pressure = 1 [atm] Reference Temperature = 25 [C] END DYNAMIC VISCOSITY: Dynamic Viscosity = 17.7E-06 [kg m^-1 s^-1] Option = Value END THERMAL CONDUCTIVITY: Option = Value

coffee husk outfiles.txt Thermal Conductivity = 259E-04 [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 END END MATERIAL: O2 Material Description = Oxygen O2 Material Group = Gas Phase Combustion Option = Pure Substance Thermodynamic State = Gas PROPERTIES: Option = General Material EQUATION OF STATE: Molar Mass = 31.99 [kg kmol^-1] Option = Ideal Gas END SPECIFIC HEAT CAPACITY: Option = NASA Format LOWER INTERVAL COEFFICIENTS: NASA a1 = 0.03212936E+02 [] NASA a2 = 0.01127486E-01 [K^-1] NASA a3 = -0.05756150E-05 [K^-2] NASA a4 = 0.01313877E-07 [K^-3] NASA a5 = -0.08768554E-11 [K^-4] NASA a6 = -0.01005249E+05 [K] NASA a7 = 0.06034738E+02 [] END TEMPERATURE LIMITS: Lower Temperature = 300 [K] Midpoint Temperature = 1000 [K] Upper Temperature = 5000 [K] END UPPER INTERVAL COEFFICIENTS: NASA a1 = 0.03697578E+02 [] NASA a2 = 0.06135197E-02 [K^-1] NASA a3 = -0.01258842E-05 [K^-2] NASA a4 = 0.01775281E-09 [K^-3] NASA a5 = -0.01136435E-13 [K^-4] NASA a6 = -0.01233930E+05 [K] NASA a7 = 0.03189166E+02 [] END END REFERENCE STATE: Option = NASA Format Reference Pressure = 1 [atm] Reference Temperature = 25 [C] END DYNAMIC VISCOSITY: Dynamic Viscosity = 19.2E-06 [kg m^-1 s^-1] Option = Value END THERMAL CONDUCTIVITY:

coffee husk outfiles.txt Option = Value Thermal Conductivity = 266E-04 [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 END END MATERIAL: Raw Combustible Material Group = Particle Solids Option = Pure Substance Thermodynamic State = Solid PROPERTIES: Option = General Material EQUATION OF STATE: Density = 1560 [kg m^-3] Molar Mass = 12 [kg kmol^-1] Option = Value END SPECIFIC HEAT CAPACITY: Option = Value Specific Heat Capacity = 1225 [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 END END REACTION: Fuel Gas Oxygen Option = Single Step Reaction Description = Fuel Gas Oxidation (kinetic data from Methane \ scaled for conserving mass rate) FORWARD REACTION RATE: Option = Arrhenius Pre Exponential Factor = 8.3E6 [s^-1] * 16 [kg kmol^-1] / Fuel Gas.mw Temperature Exponent = 0 REACTION ACTIVATION: Activation Energy = 30 [kcal mol^-1] Option = Activation Energy END END PRODUCTS: Materials List = CO2, H2O Option = Child Materials CHILD MATERIAL: CO2 Option = Fuel Analysis END CHILD MATERIAL: H2O Option = Fuel Analysis END END

coffee husk outfiles.txt REACTANTS: Materials List = Fuel Gas, O2 Option = Child Materials CHILD MATERIAL: Fuel Gas Option = Stoichiometric Reaction Order = -0.3 Stoichiometric Coefficient = 1 END CHILD MATERIAL: O2 Option = Fuel Analysis Reaction Order = 1.3 END END END REACTION: HC Fuel Char Field Material Amount Option = Mass Coefficient Option = Multi Phase Reaction Description = Field Char Oxidation HEAT RELEASE: Option = Specific Enthalpy Reference Material = Char Reference Parent Material = HC Fuel Reference Pressure = 1 [atm] Reference Specific Enthalpy = 3.408E+07 [J kg^-1] Reference Temperature = 1200 [C] END HEAT RELEASE DISTRIBUTION: Parent Materials List = HC Fuel, Gas Mixture PARENT MATERIAL: Gas Mixture Fraction of Heat Released = 0.5 Option = Fraction of Heat Released END PARENT MATERIAL: HC Fuel Fraction of Heat Released = 0.5 Option = Fraction of Heat Released END END MULTIPHASE REACTION RATE: Maximum Reaction Temperature = 3000 [K] Option = Field Char Oxidation CHAR OXIDATION RATE: Pre Exponential Factor = 497 [kg m^-2 s^-1] Temperature Exponent = 0 REACTION ACTIVATION: Activation Temperature = 8540 [K] Option = Activation Temperature END END EXTERNAL DIFFUSION: Reference Dynamic Diffusivity = 1.8E-5 [kg m^-1 s^-1] Reference Temperature = 293 [K] Temperature Exponent = 0.75 END END PRODUCTS: Option = Parent Materials Parent Materials List = Gas Mixture PARENT MATERIAL: Gas Mixture Materials List = CO2 Option = Child Materials CHILD MATERIAL: CO2 Option = Fuel Analysis END

coffee husk outfiles.txt END END REACTANTS: Option = Parent Materials Parent Materials List = HC Fuel, Gas Mixture PARENT MATERIAL: Gas Mixture Materials List = O2 Option = Child Materials CHILD MATERIAL: O2 Option = Fuel Analysis END END PARENT MATERIAL: HC Fuel Materials List = Char Option = Child Materials CHILD MATERIAL: Char Mass Coefficient = 1 Option = Mass Coefficient END END END END REACTION: HC Fuel Devolat Material Amount Option = Mass Coefficient Option = Multi Phase Reaction Description = Devolatilisation Reaction without Pollutants HEAT RELEASE: Latent Heat = 0 [J kg^-1] Option = Latent Heat Reference Material = Fuel Gas Reference Parent Material = Gas Mixture Reference Temperature = 527 [C] END HEAT RELEASE DISTRIBUTION: Parent Materials List = HC Fuel, Gas Mixture PARENT MATERIAL: Gas Mixture Fraction of Heat Released = 0 Option = Fraction of Heat Released END PARENT MATERIAL: HC Fuel Fraction of Heat Released = 1 Option = Fraction of Heat Released END END MULTIPHASE REACTION RATE: Maximum Reaction Temperature = 3000 [K] Option = Mass Arrhenius Pre Exponential Factor = 1.34E5 [s^-1] Temperature Exponent = 0 REACTION ACTIVATION: Activation Temperature = 8852 [K] Option = Activation Temperature END END PRODUCTS: Option = Parent Materials Parent Materials List = HC Fuel, Gas Mixture PARENT MATERIAL: Gas Mixture Materials List = Fuel Gas Option = Child Materials CHILD MATERIAL: Fuel Gas Option = Fuel Analysis END

coffee husk outfiles.txt END PARENT MATERIAL: HC Fuel Materials List = Char Option = Child Materials CHILD MATERIAL: Char Option = Fuel Analysis END END END REACTANTS: Option = Parent Materials Parent Materials List = HC Fuel PARENT MATERIAL: HC Fuel Materials List = Raw Combustible Option = Child Materials CHILD MATERIAL: Raw Combustible Mass Coefficient = 1 Option = Mass Coefficient Reaction Order = 1 END 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: reactor Coord Frame = Coord 0 Domain Type = Fluid Location = B9 BOUNDARY: Coffee Husk inlet Boundary Type = INLET Location = bioin BOUNDARY CONDITIONS: COMPONENT: CO2 Mass Fraction = 0.0 Option = Mass Fraction END COMPONENT: Fuel Gas Mass Fraction = 0.0 Option = Mass Fraction END COMPONENT: H2O Mass Fraction = 0.0 Option = Mass Fraction END COMPONENT: O2 Mass Fraction = 0.0 Option = Mass Fraction END

coffee husk outfiles.txt FLOW REGIME: Option = Subsonic END HEAT TRANSFER: Option = Static Temperature Static Temperature = 343 [K] END MASS AND MOMENTUM: Normal Speed = 0 [m s^-1] Option = Normal Speed END THERMAL RADIATION: Option = Local Temperature END TURBULENCE: Option = Medium Intensity and Eddy Viscosity Ratio END END FLUID: Coffee Husk BOUNDARY CONDITIONS: HEAT TRANSFER: Option = Static Temperature Static Temperature = 343 [K] END MASS AND MOMENTUM: Option = Zero Slip Velocity END PARTICLE DIAMETER DISTRIBUTION: Diameter List = 12 [m], 38 [m], 62 [m], 88 [m] Mass Fraction List = 0.18, 0.25, 0.21, 0.36 Number Fraction List = 0.25, 0.25, 0.25, 0.25 Option = Discrete Diameter Distribution END PARTICLE MASS FLOW RATE: Mass Flow Rate = 0.003469 [kg s^-1] END PARTICLE POSITION: Option = Uniform Injection Particle Locations = Equally Spaced NUMBER OF POSITIONS: Number = 200 Option = Direct Specification END END END END END BOUNDARY: airinlet Boundary Type = INLET Location = airinlet BOUNDARY CONDITIONS: COMPONENT: CO2 Mass Fraction = 0.0 Option = Mass Fraction END COMPONENT: Fuel Gas Mass Fraction = 0.0 Option = Mass Fraction END COMPONENT: H2O Mass Fraction = 0.0 Option = Mass Fraction END

coffee husk outfiles.txt COMPONENT: O2 Mass Fraction = 0.232 Option = Mass Fraction END FLOW DIRECTION: Option = Normal to Boundary Condition END FLOW REGIME: Option = Subsonic END HEAT TRANSFER: Option = Static Temperature Static Temperature = 573 [K] END MASS AND MOMENTUM: Mass Flow Rate = 0.0049 [kg s^-1] Option = Mass Flow Rate END THERMAL RADIATION: Option = Local Temperature END TURBULENCE: Option = Medium Intensity and Eddy Viscosity Ratio END END FLUID: Coffee Husk BOUNDARY CONDITIONS: END END END BOUNDARY: hopperwall Boundary Type = WALL Location = hopper wall BOUNDARY CONDITIONS: HEAT TRANSFER: Fixed Temperature = 343 [K] Option = Fixed Temperature END MASS AND MOMENTUM: Option = No Slip Wall END THERMAL RADIATION: Diffuse Fraction = 1. Emissivity = 1. Option = Opaque END WALL ROUGHNESS: Option = Smooth Wall END END FLUID: Coffee Husk BOUNDARY CONDITIONS: PARTICLE WALL INTERACTION: Option = Equation Dependent END VELOCITY: Option = Restitution Coefficient Parallel Coefficient of Restitution = 1.0 Perpendicular Coefficient of Restitution = 1.0 END END END END

coffee husk outfiles.txt BOUNDARY: outlet Boundary Type = OUTLET Location = gasout 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 THERMAL RADIATION: Option = Local Temperature END END END BOUNDARY: reactorwall Boundary Type = WALL Location = reactorwall BOUNDARY CONDITIONS: HEAT TRANSFER: Fixed Temperature = 800 [K] Option = Fixed Temperature END MASS AND MOMENTUM: Option = No Slip Wall END THERMAL RADIATION: Diffuse Fraction = 1. Emissivity = 1. Option = Opaque END WALL ROUGHNESS: Option = Smooth Wall END END FLUID: Coffee Husk BOUNDARY CONDITIONS: PARTICLE WALL INTERACTION: Option = Equation Dependent END VELOCITY: Option = Restitution Coefficient Parallel Coefficient of Restitution = 1.0 Perpendicular Coefficient of Restitution = 1.0 END END END END DOMAIN MODELS: BUOYANCY MODEL: Buoyancy Reference Density = 0.955 [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

coffee husk outfiles.txt END DOMAIN MOTION: Option = Stationary END MESH DEFORMATION: Option = None END REFERENCE PRESSURE: Reference Pressure = 1 [atm] END END FLUID DEFINITION: Coffee Husk Material = HC Fuel Option = Material Library MORPHOLOGY: Option = Dispersed Particle Transport Solid PARTICLE DIAMETER CHANGE: Option = Mass Equivalent END END END FLUID DEFINITION: Gas Mixture Material = Gas Mixture Option = Material Library MORPHOLOGY: Option = Continuous Fluid END END FLUID MODELS: COMBUSTION MODEL: Option = Fluid Dependent END FLUID: Coffee Husk EROSION MODEL: Option = None END FLUID BUOYANCY MODEL: Option = Density Difference END HEAT TRANSFER MODEL: Option = Particle Temperature END END FLUID: Gas Mixture COMBUSTION MODEL: Option = Finite Rate Chemistry and Eddy Dissipation END COMPONENT: CO2 Option = Automatic END COMPONENT: Fuel Gas Option = Automatic END COMPONENT: H2O Option = Automatic END COMPONENT: N2 Option = Constraint END COMPONENT: O2 Option = Automatic END FLUID BUOYANCY MODEL:

coffee husk outfiles.txt Option = Density Difference END HEAT TRANSFER MODEL: Option = Thermal Energy END THERMAL RADIATION MODEL: Option = Discrete Transfer Radiation Transfer Mode = Participating Media SCATTERING MODEL: Option = None END SPECTRAL MODEL: Option = Gray END END END HEAT TRANSFER MODEL: Option = Fluid Dependent END THERMAL RADIATION MODEL: Option = Fluid Dependent END TURBULENCE MODEL: Option = k epsilon BUOYANCY TURBULENCE: Option = None END END TURBULENT WALL FUNCTIONS: Option = Scalable END END FLUID PAIR: Gas Mixture | Coffee Husk Particle Coupling = Fully Coupled INTERPHASE HEAT TRANSFER: Option = Ranz Marshall END INTERPHASE THERMAL RADIATION: Emissivity = 1. Option = Opaque Particle Coupling = Fully Coupled END MOMENTUM TRANSFER: DRAG FORCE: Option = Schiller Naumann END PRESSURE GRADIENT FORCE: Option = None END TURBULENT DISPERSION FORCE: Option = None END VIRTUAL MASS FORCE: Option = None END END END MULTIPHASE MODELS: MULTIPHASE REACTIONS: Reactions List = HC Fuel Char Field,HC Fuel Devolat END END END

coffee husk outfiles.txt 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: Maximum Number of Iterations = 600 Minimum Number of Iterations = 1 Physical Timescale = 0.005 [s] Timescale Control = Physical Timescale END CONVERGENCE CRITERIA: Residual Target = 1.E-4 Residual Type = RMS END DYNAMIC MODEL CONTROL: Global Dynamic Model Control = On END PARTICLE CONTROL: PARTICLE INTEGRATION: First Iteration for Particle Calculation = 25 Iteration Frequency = 10 Option = Forward Euler END PARTICLE UNDER RELAXATION FACTORS: Energy Under Relaxation Factor = 0.75 Mass Under Relaxation Factor = 0.75 Velocity Under Relaxation Factor = 0.75 END END THERMAL RADIATION CONTROL: COARSENING CONTROL: Target Coarsening Rate = 16 END END END END COMMAND FILE: Version = 12.1 Results Version = 12.1 END SIMULATION CONTROL: EXECUTION CONTROL: EXECUTABLE SELECTION: Double Precision = On END INTERPOLATOR STEP CONTROL: Runtime Priority = Standard MEMORY CONTROL: Memory Allocation Factor = 1.0 END END PARALLEL HOST LIBRARY: HOST DEFINITION: usere0d9062d4b Remote Host Name = USER-E0D9062D4B Host Architecture String = winnt Installation Root = C:\Program Files\ANSYS Inc\v%v\CFX

coffee husk outfiles.txt 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:\Documents and Settings\User\Local \ Settings\Temp\coffee husk \ gasifier_2396_Working\dp0\CFX\CFX\Work1\Fluid Flow.def END SOLVER STEP CONTROL: Runtime Priority = Standard EXECUTABLE SELECTION: Double Precision = On END 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 12.1 | | | | Version 2009.10.15-23.08 Fri Oct 16 02:45:02 GMTDT 2009 | | | | Executable Attributes | | | | double-int32-32bit-novc8-noifort-novc6-optimised-supfort-noprof-nos| | | | Copyright 2009 ANSYS Inc. | +--------------------------------------------------------------------+

coffee husk outfiles.txt

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

Run mode: serial run

Host computer: USER-E0D9062D4B Job started: Wed Jun 20 16:57:36 2012

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

Data Type Kwords Words/Node Words/Elem Kbytes Bytes/Node Real 9764.5 3234.35 712.74 76285.1 25874.77 Integer 2350.7 778.63 171.58 9182.4 3114.53 Character 3895.4 1290.29 284.33 3804.1 1290.29 Logical 65.0 21.53 4.74 253.9 86.12 Double 8.0 2.65 0.58 62.5 21.20

+--------------------------------------------------------------------+ | ****** Notice ****** | | Wall Heat Transfer Coefficient written to the results file uses | | "Wall Adjacent Temperature" for the bulk temperature. If you want | | to override the bulk temperature then set the expert parameter | | "tbulk for htc = <value>" | +--------------------------------------------------------------------+

+--------------------------------------------------------------------+ | Radiation Coarsening Information | +--------------------------------------------------------------------+

Domain Name : reactor

Target coarsening rate = 16 Number of fine grid elements = 13700 Number of radiation elements = 2293 Actual coarsening rate = 5

+--------------------------------------------------------------------+ | Mesh Statistics | +--------------------------------------------------------------------+ | Domain Name | Orthog. Angle | Exp. Factor | Aspect Ratio | +----------------------+---------------+--------------+--------------+ | | Minimum [deg] | Maximum | Maximum | +----------------------+---------------+--------------+--------------+ | reactor | 38.5 ok | 19 ok | 9 OK | +----------------------+---------------+--------------+--------------+ | | %! %ok %OK | %! %ok %OK | %! %ok %OK | +----------------------+---------------+--------------+--------------+ | reactor | 0 <1 100 | 0 1 99 | 0 0 100 | +----------------------+---------------+--------------+--------------+

Domain Name : reactor

Total Number of Nodes = 3019

coffee husk outfiles.txt Total Number of Elements = 13700 Total Number of Tetrahedrons = 13700

Total Number of Faces = 2676

+--------------------------------------------------------------------+ | Buoyancy Reference Information | +--------------------------------------------------------------------+

Domain Group: reactor Buoyancy has been activated. The absolute pressure will include hydrostatic pressure contribution, using the following reference coordinates: ( 1.58333E-06, 1.20000E+00,-1.37583E-05).

====================================================================== HC Fuel Proximate/Ultimate Analysis ======================================================================

Initial mass fractions for particle : HC Fuel Ash = 6.8000E-03 Char = 0.0000E+00 Raw Combustible = 9.9320E-01

Volatiles material properties : Fuel Gas Molar Mass [kg/kmol] = 20.614 Ref. Spec. Enthalpy (p= 1.01325E+05, T= 2.98150E+02) = -6.6036E+06

+--------------------------------------------------------------------+ | Autocomputed Stoichiometric Coefficients | +--------------------------------------------------------------------+

Reaction (volatiles oxidation) : Fuel Gas Oxygen Reactants: Fuel Gas = 1.0000E+00 O2 = 8.2469E-01 Products: CO2 = 7.7858E-01 H2O = 7.0815E-01

+--------------------------------------------------------------------+ | Autocomputed Mass Coefficients | +--------------------------------------------------------------------+

Reaction (devolatilisation) : HC Fuel Devolat Reactants: HC Fuel.Raw Combustible = 1.0000E+00 Products: HC Fuel.Char = 3.5812E-02 Gas Mixture.Fuel Gas = 1.0358E+00

Reaction (char oxidation) : HC Fuel Char Field Reactants: HC Fuel.Char = 1.0000E+00 Gas Mixture.O2 = 2.6667E+00 Products: Gas Mixture.CO2 = 3.6667E+00

+--------------------------------------------------------------------+ | Single Step Reactions Heat Release | +--------------------------------------------------------------------+

Enthalpy per [mol] of reaction at reference conditionsPage 20

coffee husk outfiles.txt (Pressure= 1.01325E+05, Temperature= 2.98150E+02)

Fuel Gas Oxygen = 3.4155E+05

+--------------------------------------------------------------------+ | Multi-Component Specific Enthalpy Diffusion | +--------------------------------------------------------------------+

Unity Lewis Number (Le=1) for multi-component specific enthalpy diffusion applied for fluids below.

Domain Name : reactor Gas Mixture

+--------------------------------------------------------------------+ | Average Scale Information | +--------------------------------------------------------------------+

Domain Name : reactor Global Length = 3.3614E-01 Minimum Extent = 2.0000E-01 Maximum Extent = 1.2000E+00 Density = 4.4389E-01 Dynamic Viscosity = 1.7700E-05 Velocity = 2.6645E-01 Advection Time = 1.2615E+00 Reynolds Number = 2.2461E+03 Speed of Sound = 5.5798E+02 Mach Number = 4.7753E-04 Thermal Conductivity = 2.5900E-02 Specific Heat Capacity at Constant Pressure = 1.1127E+03 Specific Heat Capacity at Constant Volume = 8.1586E+02 Specific Heat Ratio = 1.3638E+00 Prandtl Number = 7.6042E-01 Total Extinction Coefficient = 1.0000E+00 Optical Thickness = 3.3614E-01

+--------------------------------------------------------------------+ | Checking for Isolated Fluid Regions | +--------------------------------------------------------------------+ No isolated fluid regions were found.

+--------------------------------------------------------------------+ | The Equations Solved in This Calculation | +--------------------------------------------------------------------+

Subsystem : Momentum and Mass

U-Mom V-Mom W-Mom P-Mass

Subsystem : Thermal Radiation

I-Radiation

Subsystem : Heat Transfer

H-Energy

Subsystem : TurbKE and Diss.KPage 21

K-TurbKE E-Diss.K

Subsystem : Mass Fractions

Fuel Gas-Mass Fraction O2-Mass Fraction CO2-Mass Fraction H2O-Mass Fraction

+--------------------------------------------------------------------+ | Particle Transport Equations Solved in This Calculation | +--------------------------------------------------------------------+

Domain Type : reactor Mass-Char-Coffee Husk Mass-Raw Combustible-Coffee Husk x-Mom-Coffee Husk y-Mom-Coffee Husk z-Mom-Coffee Husk Energy-Coffee Husk CFD Solver started: Wed Jun 20 16:57:40 2012

+--------------------------------------------------------------------+ | Convergence History | +--------------------------------------------------------------------+

====================================================================== | Timescale Information | ---------------------------------------------------------------------- | Equation | Type | Timescale | +----------------------+------------------------+--------------------+ | U-Mom | Physical Timescale | 5.00000E-03 | | V-Mom | Physical Timescale | 5.00000E-03 | | W-Mom | Physical Timescale | 5.00000E-03 | | P-Mass | Physical Timescale | 5.00000E-03 | +----------------------+------------------------+--------------------+ | H-Energy | Physical Timescale | 5.00000E-03 | +----------------------+------------------------+--------------------+ | K-TurbKE | Physical Timescale | 5.00000E-03 | | E-Diss.K | Physical Timescale | 5.00000E-03 | +----------------------+------------------------+--------------------+ | Fuel Gas-Mass Fracti | Physical Timescale | 5.00000E-03 | | O2-Mass Fraction | Physical Timescale | 5.00000E-03 | | CO2-Mass Fraction | Physical Timescale | 5.00000E-03 | | H2O-Mass Fraction | Physical Timescale | 5.00000E-03 | +----------------------+------------------------+--------------------+

====================================================================== OUTER LOOP ITERATION = 1 CPU SECONDS = 8.594E-01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 0.00 | 1.0E-04 | 7.3E-04 | 6.4E+01 ok| | V-Mom | 0.00 | 1.4E+00 | 2.4E+00 | 1.4E-03 OK| | W-Mom | 0.00 | 1.6E-02 | 1.2E-01 | 2.6E-01 ok| | P-Mass | 0.00 | 2.3E-02 | 1.6E-01 | 8.5 5.9E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 |

coffee husk outfiles.txt +----------------------+------+---------+---------+------------------+ | H-Energy | 0.00 | 2.9E-01 | 2.0E+00 | 5.3 5.0E-09 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.00 | 1.3E-01 | 1.7E+00 | 5.3 1.5E-08 OK| | E-Diss.K | 0.00 | 2.6E+00 | 7.1E+00 | 12.0 3.2E-15 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | O2-Mass Fraction | 0.00 | 2.9E-01 | 2.1E+00 | 5.3 4.9E-09 OK| | CO2-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | H2O-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 2 CPU SECONDS = 2.719E+00 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom |99.99 | 4.5E-02 | 3.7E-01 | 5.0E-02 OK| | V-Mom | 0.73 | 1.0E+00 | 2.1E+00 | 7.1E-04 OK| | W-Mom |13.15 | 2.0E-01 | 9.9E-01 | 3.9E-03 OK| | P-Mass | 0.25 | 5.8E-03 | 4.8E-02 | 8.5 8.2E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.58 | 1.7E-01 | 1.3E+00 | 5.3 6.6E-09 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.72 | 2.3E-01 | 2.9E+00 | 5.3 2.1E-08 OK| | E-Diss.K | 0.11 | 2.8E-01 | 3.4E+00 | 12.0 6.3E-15 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | O2-Mass Fraction | 0.58 | 1.7E-01 | 1.3E+00 | 5.3 6.4E-09 OK| | CO2-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | H2O-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 3 CPU SECONDS = 3.672E+00 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 0.75 | 3.3E-02 | 2.2E-01 | 2.5E-02 OK| | V-Mom | 0.80 | 8.0E-01 | 1.6E+00 | 2.1E-04 OK| | W-Mom | 0.81 | 1.7E-01 | 7.2E-01 | 1.7E-03 OK| | P-Mass | 0.13 | 7.5E-04 | 7.7E-03 | 38.5 9.6E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.76 | 1.3E-01 | 9.9E-01 | 5.3 8.6E-09 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.95 | 2.2E-01 | 2.7E+00 | 5.3 2.8E-08 OK| | E-Diss.K | 0.97 | 2.7E-01 | 3.6E+00 | 12.0 1.1E-14 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | O2-Mass Fraction | 0.75 | 1.3E-01 | 1.0E+00 | 5.3 8.4E-09 OK| | CO2-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | H2O-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 4 CPU SECONDS = 4.703E+00 ----------------------------------------------------------------------

coffee husk outfiles.txt | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 0.66 | 2.2E-02 | 1.3E-01 | 4.4E-02 OK| | V-Mom | 0.62 | 4.9E-01 | 1.1E+00 | 6.8E-04 OK| | W-Mom | 0.66 | 1.1E-01 | 4.1E-01 | 4.7E-03 OK| | P-Mass | 0.80 | 6.0E-04 | 3.3E-03 | 23.5 9.9E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.81 | 1.0E-01 | 8.0E-01 | 5.3 1.4E-08 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.80 | 1.8E-01 | 2.1E+00 | 5.3 3.5E-08 OK| | E-Diss.K | 0.79 | 2.2E-01 | 2.9E+00 | 12.0 3.7E-14 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | O2-Mass Fraction | 0.81 | 1.0E-01 | 8.2E-01 | 5.3 1.4E-08 OK| | CO2-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | H2O-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 5 CPU SECONDS = 5.656E+00 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 0.67 | 1.5E-02 | 8.8E-02 | 4.0E-02 OK| | V-Mom | 0.60 | 2.9E-01 | 7.6E-01 | 9.3E-04 OK| | W-Mom | 0.58 | 6.4E-02 | 2.0E-01 | 6.4E-03 OK| | P-Mass | 0.80 | 4.9E-04 | 3.2E-03 | 23.5 8.8E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.86 | 9.0E-02 | 6.8E-01 | 5.3 2.6E-08 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.75 | 1.3E-01 | 1.5E+00 | 5.3 5.2E-08 OK| | E-Diss.K | 0.79 | 1.7E-01 | 2.2E+00 | 12.0 1.0E-13 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | O2-Mass Fraction | 0.86 | 9.0E-02 | 7.0E-01 | 5.3 2.4E-08 OK| | CO2-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | H2O-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 6 CPU SECONDS = 6.625E+00 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 0.74 | 1.1E-02 | 5.7E-02 | 4.3E-02 OK| | V-Mom | 0.53 | 1.6E-01 | 5.0E-01 | 1.8E-03 OK| | W-Mom | 0.58 | 3.7E-02 | 1.4E-01 | 1.0E-02 OK| | P-Mass | 0.84 | 4.1E-04 | 2.8E-03 | 19.7 8.9E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.90 | 8.1E-02 | 5.8E-01 | 5.3 4.4E-08 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.75 | 9.9E-02 | 1.0E+00 | 5.3 1.0E-07 OK| | E-Diss.K | 0.84 | 1.4E-01 | 1.9E+00 | 12.0 2.8E-13 OK| +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt | Fuel Gas-Mass Fracti | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | O2-Mass Fraction | 0.90 | 8.1E-02 | 6.1E-01 | 5.3 4.0E-08 OK| | CO2-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | H2O-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 7 CPU SECONDS = 7.609E+00 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 0.75 | 8.2E-03 | 4.5E-02 | 5.1E-02 OK| | V-Mom | 0.46 | 7.2E-02 | 3.2E-01 | 4.7E-03 OK| | W-Mom | 0.57 | 2.1E-02 | 1.0E-01 | 1.7E-02 OK| | P-Mass | 0.82 | 3.4E-04 | 2.4E-03 | 16.0 9.9E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.92 | 7.5E-02 | 5.2E-01 | 5.3 8.1E-08 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.76 | 7.6E-02 | 7.3E-01 | 5.3 1.8E-07 OK| | E-Diss.K | 0.80 | 1.1E-01 | 2.0E+00 | 12.0 7.3E-13 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | O2-Mass Fraction | 0.93 | 7.5E-02 | 5.4E-01 | 5.3 7.3E-08 OK| | CO2-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | H2O-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 9 CPU SECONDS = 9.484E+00 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 0.84 | 5.4E-03 | 3.1E-02 | 5.7E-02 OK| | V-Mom | 1.41 | 6.1E-02 | 1.4E-01 | 2.3E-03 OK| | W-Mom | 0.74 | 9.2E-03 | 6.1E-02 | 3.5E-02 OK| | P-Mass | 0.85 | 2.3E-04 | 2.0E-03 | 12.2 8.8E-02 OK|

coffee husk outfiles.txt +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.95 | 6.7E-02 | 4.5E-01 | 5.3 1.2E-07 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.81 | 4.8E-02 | 4.1E-01 | 5.3 6.3E-07 OK| | E-Diss.K | 0.82 | 7.1E-02 | 1.4E+00 | 12.0 2.7E-12 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | O2-Mass Fraction | 0.96 | 6.7E-02 | 4.6E-01 | 5.3 1.0E-07 OK| | CO2-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | H2O-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt ====================================================================== OUTER LOOP ITERATION = 12 CPU SECONDS = 1.223E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 0.99 | 4.5E-03 | 3.2E-02 | 3.4E-02 OK| | V-Mom | 1.05 | 9.4E-02 | 2.1E-01 | 9.5E-04 OK| | W-Mom | 1.04 | 9.7E-03 | 4.3E-02 | 1.1E-02 OK| | P-Mass | 0.88 | 1.5E-04 | 1.5E-03 | 4.7 7.0E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.97 | 6.0E-02 | 3.9E-01 | 5.3 2.5E-07 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.87 | 3.0E-02 | 2.2E-01 | 5.3 9.7E-07 OK| | E-Diss.K | 0.89 | 4.7E-02 | 8.6E-01 | 12.0 3.2E-12 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | O2-Mass Fraction | 0.97 | 6.1E-02 | 4.1E-01 | 5.3 2.2E-07 OK| | CO2-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | H2O-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 13 CPU SECONDS = 1.316E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 1.01 | 4.6E-03 | 3.2E-02 | 1.8E-02 OK| | V-Mom | 1.03 | 9.7E-02 | 2.2E-01 | 1.0E-03 OK| | W-Mom | 1.02 | 1.0E-02 | 4.2E-02 | 7.4E-03 OK| | P-Mass | 0.88 | 1.3E-04 | 1.4E-03 | 4.7 6.5E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.97 | 5.8E-02 | 3.9E-01 | 5.3 2.4E-07 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.89 | 2.7E-02 | 2.0E-01 | 5.3 9.4E-07 OK| | E-Diss.K | 0.90 | 4.2E-02 | 7.4E-01 | 12.0 4.7E-12 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | O2-Mass Fraction | 0.98 | 6.0E-02 | 4.2E-01 | 5.3 2.1E-07 OK| | CO2-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | H2O-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 14 CPU SECONDS = 1.405E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 1.02 | 4.7E-03 | 3.2E-02 | 2.5E-02 OK| | V-Mom | 1.01 | 9.8E-02 | 2.2E-01 | 6.4E-04 OK| | W-Mom | 1.00 | 9.9E-03 | 4.2E-02 | 9.1E-03 OK| | P-Mass | 0.89 | 1.2E-04 | 1.3E-03 | 8.5 7.5E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.98 | 5.7E-02 | 3.8E-01 | 5.3 2.6E-07 OK| +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt | K-TurbKE | 0.90 | 2.4E-02 | 1.7E-01 | 5.3 9.4E-07 OK| | E-Diss.K | 0.90 | 3.8E-02 | 6.4E-01 | 12.0 4.1E-12 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | O2-Mass Fraction | 0.98 | 5.8E-02 | 4.1E-01 | 5.3 2.3E-07 OK| | CO2-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | H2O-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 17 CPU SECONDS = 1.680E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 1.00 | 4.7E-03 | 3.7E-02 | 2.2E-02 OK|

coffee husk outfiles.txt | V-Mom | 0.84 | 7.1E-02 | 1.9E-01 | 7.0E-04 OK| | W-Mom | 0.97 | 9.0E-03 | 4.0E-02 | 9.9E-03 OK| | P-Mass | 0.92 | 9.1E-05 | 1.0E-03 | 16.0 8.6E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.98 | 5.4E-02 | 3.6E-01 | 5.3 2.1E-07 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.93 | 1.8E-02 | 1.1E-01 | 5.3 4.4E-07 OK| | E-Diss.K | 0.92 | 2.9E-02 | 4.3E-01 | 12.0 1.2E-12 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | O2-Mass Fraction | 0.98 | 5.5E-02 | 3.9E-01 | 5.3 1.9E-07 OK| | CO2-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | H2O-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 19 CPU SECONDS = 1.869E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 0.95 | 4.4E-03 | 3.7E-02 | 2.2E-02 OK| | V-Mom | 0.87 | 5.2E-02 | 1.8E-01 | 9.2E-04 OK| | W-Mom | 0.94 | 8.1E-03 | 4.0E-02 | 1.0E-02 OK| | P-Mass | 0.92 | 7.7E-05 | 9.2E-04 | 12.2 9.2E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.98 | 5.2E-02 | 3.4E-01 | 5.3 1.6E-07 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.94 | 1.6E-02 | 9.6E-02 | 5.3 3.2E-07 OK| | E-Diss.K | 0.93 | 2.5E-02 | 3.4E-01 | 12.0 6.5E-13 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | O2-Mass Fraction | 0.98 | 5.3E-02 | 3.7E-01 | 5.3 1.5E-07 OK| | CO2-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK|

coffee husk outfiles.txt | H2O-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 22 CPU SECONDS = 2.148E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 0.92 | 3.6E-03 | 2.9E-02 | 2.2E-02 OK| | V-Mom | 0.90 | 3.5E-02 | 1.5E-01 | 1.3E-03 OK| | W-Mom | 0.92 | 6.4E-03 | 3.6E-02 | 1.1E-02 OK| | P-Mass | 0.92 | 6.0E-05 | 7.5E-04 | 8.5 9.7E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 |

coffee husk outfiles.txt +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 4.9E-02 | 3.0E-01 | 5.3 1.1E-07 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.96 | 1.4E-02 | 9.0E-02 | 5.3 9.6E-08 OK| | E-Diss.K | 0.93 | 2.0E-02 | 2.4E-01 | 12.0 2.0E-13 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | O2-Mass Fraction | 0.99 | 5.1E-02 | 3.3E-01 | 5.3 1.1E-07 OK| | CO2-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | H2O-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 0.92 | 2.8E-03 | 2.4E-02 | 1.9E-02 OK| | V-Mom | 0.90 | 2.5E-02 | 1.3E-01 | 1.3E-03 OK| | W-Mom | 0.92 | 5.0E-03 | 2.9E-02 | 1.0E-02 OK| | P-Mass | 0.93 | 4.8E-05 | 6.1E-04 | 8.5 8.1E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 4.8E-02 | 2.8E-01 | 5.3 7.4E-08 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.96 | 1.3E-02 | 8.3E-02 | 5.3 1.1E-08 OK| | E-Diss.K | 0.94 | 1.7E-02 | 1.7E-01 | 12.0 7.0E-14 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | O2-Mass Fraction | 0.99 | 4.9E-02 | 3.2E-01 | 5.3 7.2E-08 OK| | CO2-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| | H2O-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| +----------------------+------+---------+---------+------------------+

====================================================================== Particle Diagnostics ======================================================================

====================================================================== OUTER LOOP ITERATION = 26 CPU SECONDS = 2.523E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 0.92 | 2.6E-03 | 2.3E-02 | 1.7E-02 OK| | V-Mom | 0.90 | 2.2E-02 | 1.2E-01 | 1.3E-03 OK|

coffee husk outfiles.txt | W-Mom | 0.92 | 4.6E-03 | 2.7E-02 | 9.1E-03 OK| | P-Mass | 0.93 | 4.4E-05 | 5.7E-04 | 8.5 7.2E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 4.7E-02 | 2.8E-01 | 5.3 6.5E-08 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.97 | 1.2E-02 | 8.0E-02 | 5.3 1.1E-08 OK| | E-Diss.K | 0.94 | 1.6E-02 | 1.6E-01 | 12.0 4.2E-14 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.00 | 3.2E-01 | 7.8E+00 | 5.3 2.2E-09 OK| | O2-Mass Fraction | 0.99 | 4.9E-02 | 3.1E-01 | 5.3 6.3E-08 OK| | CO2-Mass Fraction | 0.00 | 5.8E-36 | 1.6E-34 | 5.3 0.0E+00 OK| | H2O-Mass Fraction | 0.00 | 0.0E+00 | 0.0E+00 | 5.3 0.0E+00 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 27 CPU SECONDS = 2.616E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 0.92 | 2.4E-03 | 2.2E-02 | 1.8E-02 OK| | V-Mom | 0.91 | 2.0E-02 | 1.1E-01 | 2.9E-03 OK| | W-Mom | 0.92 | 4.2E-03 | 2.5E-02 | 1.1E-02 OK| | P-Mass | 0.93 | 4.1E-05 | 5.3E-04 | 4.7 9.5E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 4.6E-02 | 2.7E-01 | 5.3 5.6E-08 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.97 | 1.2E-02 | 7.7E-02 | 5.3 1.8E-08 OK| | E-Diss.K | 0.94 | 1.5E-02 | 1.5E-01 | 12.0 2.4E-14 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.49 | 1.6E-01 | 3.7E+00 | 5.3 1.9E-09 OK| | O2-Mass Fraction | 0.99 | 4.8E-02 | 3.1E-01 | 5.3 5.4E-08 OK| | CO2-Mass Fraction | 0.00 | 2.6E-01 | 8.2E+00 | 5.3 6.5E-10 OK| | H2O-Mass Fraction | 0.00 | 2.6E-01 | 8.2E+00 | 5.3 6.5E-10 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 28 CPU SECONDS = 2.708E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 0.92 | 2.2E-03 | 2.1E-02 | 1.5E-02 OK| | V-Mom | 0.95 | 1.9E-02 | 1.1E-01 | 1.3E-03 OK| | W-Mom | 0.93 | 3.9E-03 | 2.2E-02 | 8.4E-03 OK| | P-Mass | 0.93 | 3.8E-05 | 5.0E-04 | 8.5 6.7E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 4.6E-02 | 2.7E-01 | 5.3 4.4E-08 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.97 | 1.1E-02 | 7.4E-02 | 5.3 2.3E-08 OK| | E-Diss.K | 0.94 | 1.4E-02 | 1.5E-01 | 12.0 2.8E-14 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.66 | 1.0E-01 | 2.5E+00 | 5.3 2.0E-09 OK| | O2-Mass Fraction | 0.99 | 4.8E-02 | 3.0E-01 | 5.3 4.3E-08 OK| | CO2-Mass Fraction | 0.99 | 2.6E-01 | 4.4E+00 | 5.3 5.6E-10 OK| | H2O-Mass Fraction | 0.99 | 2.6E-01 | 4.4E+00 | 5.3 5.6E-10 OK|

coffee husk outfiles.txt +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 31 CPU SECONDS = 2.989E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 0.94 | 1.8E-03 | 1.7E-02 | 1.5E-02 OK| | V-Mom | 0.92 | 1.6E-02 | 9.8E-02 | 3.4E-03 OK| | W-Mom | 0.92 | 3.1E-03 | 1.7E-02 | 9.8E-03 OK| | P-Mass | 0.93 | 3.1E-05 | 4.0E-04 | 4.7 8.7E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt | H-Energy | 0.99 | 4.5E-02 | 2.5E-01 | 5.3 2.6E-08 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.97 | 1.0E-02 | 7.0E-02 | 5.3 2.1E-08 OK| | E-Diss.K | 0.94 | 1.1E-02 | 1.3E-01 | 12.0 7.8E-15 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.84 | 5.2E-02 | 1.3E+00 | 5.3 1.6E-09 OK| | O2-Mass Fraction | 0.99 | 4.7E-02 | 2.8E-01 | 5.3 2.5E-08 OK| | CO2-Mass Fraction | 0.93 | 1.5E-01 | 3.4E+00 | 5.3 3.7E-10 OK| | H2O-Mass Fraction | 0.93 | 1.5E-01 | 3.4E+00 | 5.3 3.7E-10 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 33 CPU SECONDS = 3.169E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 0.95 | 1.6E-03 | 1.4E-02 | 1.1E-02 OK| | V-Mom | 0.97 | 1.5E-02 | 9.2E-02 | 1.3E-03 OK| | W-Mom | 0.94 | 2.7E-03 | 1.6E-02 | 6.7E-03 OK| | P-Mass | 0.93 | 2.7E-05 | 3.5E-04 | 8.5 5.4E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 4.4E-02 | 2.5E-01 | 5.3 1.9E-08 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.97 | 9.8E-03 | 6.8E-02 | 5.3 1.7E-08 OK| | E-Diss.K | 0.94 | 1.0E-02 | 1.1E-01 | 12.0 3.8E-15 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.88 | 4.0E-02 | 9.5E-01 | 5.3 1.3E-09 OK| | O2-Mass Fraction | 0.99 | 4.6E-02 | 2.8E-01 | 5.3 1.8E-08 OK| | CO2-Mass Fraction | 0.85 | 1.1E-01 | 2.6E+00 | 5.3 4.1E-10 OK| | H2O-Mass Fraction | 0.85 | 1.1E-01 | 2.6E+00 | 5.3 4.1E-10 OK| +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt +----------------------+------+---------+---------+------------------+ | U-Mom | 0.96 | 1.5E-03 | 1.3E-02 | 1.4E-02 OK| | V-Mom | 0.94 | 1.4E-02 | 8.7E-02 | 3.7E-03 OK| | W-Mom | 0.94 | 2.6E-03 | 1.6E-02 | 9.6E-03 OK| | P-Mass | 0.94 | 2.5E-05 | 3.2E-04 | 4.7 8.7E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 4.4E-02 | 2.4E-01 | 5.3 1.6E-08 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.98 | 9.5E-03 | 6.8E-02 | 5.3 1.6E-08 OK| | E-Diss.K | 0.94 | 9.6E-03 | 1.1E-01 | 12.0 2.6E-15 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.90 | 3.6E-02 | 8.5E-01 | 5.3 1.2E-09 OK| | O2-Mass Fraction | 0.99 | 4.6E-02 | 2.7E-01 | 5.3 1.6E-08 OK| | CO2-Mass Fraction | 0.90 | 9.4E-02 | 2.3E+00 | 5.3 3.8E-10 OK| | H2O-Mass Fraction | 0.90 | 9.4E-02 | 2.3E+00 | 5.3 3.8E-10 OK| +----------------------+------+---------+---------+------------------+

+--------------------------------------------------------------------+ | Particle Equation | Total source and source change rates | +--------------------------------------------------------------------+ | | Equation Source Rate | +--------------------------------------------------------------------+ | Domain: reactor |

====================================================================== OUTER LOOP ITERATION = 40 CPU SECONDS = 3.828E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 0.99 | 1.4E-03 | 1.1E-02 | 7.4E-03 OK| | V-Mom | 1.00 | 1.2E-02 | 8.0E-02 | 1.3E-03 OK| | W-Mom | 1.00 | 2.3E-03 | 1.5E-02 | 4.8E-03 OK| | P-Mass | 0.94 | 1.8E-05 | 2.1E-04 | 8.5 4.4E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 4.2E-02 | 2.4E-01 | 5.3 6.3E-09 OK|

coffee husk outfiles.txt +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.98 | 8.5E-03 | 6.3E-02 | 5.3 8.5E-09 OK| | E-Diss.K | 0.95 | 7.0E-03 | 7.3E-02 | 12.0 6.5E-16 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.93 | 2.8E-02 | 6.5E-01 | 5.3 6.1E-10 OK| | O2-Mass Fraction | 1.00 | 4.4E-02 | 2.7E-01 | 5.3 6.2E-09 OK| | CO2-Mass Fraction | 1.02 | 8.3E-02 | 1.8E+00 | 5.3 2.1E-10 OK| | H2O-Mass Fraction | 1.02 | 8.3E-02 | 1.8E+00 | 5.3 2.1E-10 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 43 CPU SECONDS = 4.108E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt | U-Mom | 1.01 | 1.4E-03 | 1.1E-02 | 1.6E-02 OK| | V-Mom | 0.97 | 1.1E-02 | 7.5E-02 | 4.2E-03 OK| | W-Mom | 1.03 | 2.4E-03 | 1.5E-02 | 1.0E-02 OK| | P-Mass | 0.97 | 1.6E-05 | 1.6E-04 | 4.7 9.9E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 4.1E-02 | 2.3E-01 | 5.3 4.2E-09 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.99 | 8.1E-03 | 5.8E-02 | 5.3 5.0E-09 OK| | E-Diss.K | 0.96 | 6.2E-03 | 6.9E-02 | 12.0 2.0E-16 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.95 | 2.3E-02 | 5.3E-01 | 5.3 4.1E-10 OK| | O2-Mass Fraction | 1.00 | 4.4E-02 | 2.6E-01 | 5.3 4.2E-09 OK| | CO2-Mass Fraction | 1.03 | 8.9E-02 | 2.1E+00 | 5.3 1.8E-10 OK| | H2O-Mass Fraction | 1.03 | 8.9E-02 | 2.1E+00 | 5.3 1.8E-10 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 45 CPU SECONDS = 4.295E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 1.01 | 1.4E-03 | 1.1E-02 | 6.8E-03 OK| | V-Mom | 0.97 | 1.1E-02 | 7.2E-02 | 1.2E-03 OK| | W-Mom | 1.04 | 2.6E-03 | 1.4E-02 | 4.4E-03 OK| | P-Mass | 0.98 | 1.5E-05 | 1.3E-04 | 8.5 4.1E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 4.1E-02 | 2.2E-01 | 5.3 3.1E-09 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.99 | 7.9E-03 | 5.5E-02 | 5.3 5.1E-09 OK| | E-Diss.K | 0.96 | 5.7E-03 | 6.5E-02 | 12.0 1.3E-16 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.96 | 2.1E-02 | 4.7E-01 | 5.3 3.5E-10 OK| | O2-Mass Fraction | 1.00 | 4.3E-02 | 2.5E-01 | 5.3 3.1E-09 OK|

coffee husk outfiles.txt | CO2-Mass Fraction | 1.01 | 9.3E-02 | 2.0E+00 | 5.3 1.4E-10 OK| | H2O-Mass Fraction | 1.01 | 9.3E-02 | 2.0E+00 | 5.3 1.4E-10 OK| +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt ====================================================================== OUTER LOOP ITERATION = 47 CPU SECONDS = 4.488E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 1.01 | 1.4E-03 | 1.1E-02 | 8.1E-03 OK| | V-Mom | 1.02 | 1.1E-02 | 7.1E-02 | 1.3E-03 OK| | W-Mom | 1.03 | 2.7E-03 | 1.4E-02 | 5.1E-03 OK| | P-Mass | 0.94 | 1.3E-05 | 1.1E-04 | 8.5 4.9E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 4.0E-02 | 2.1E-01 | 5.3 2.6E-09 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.99 | 7.8E-03 | 5.2E-02 | 5.3 4.2E-09 OK| | E-Diss.K | 0.97 | 5.3E-03 | 6.1E-02 | 12.0 1.2E-16 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.96 | 2.1E-02 | 4.6E-01 | 5.3 3.2E-10 OK| | O2-Mass Fraction | 1.00 | 4.3E-02 | 2.4E-01 | 5.3 2.6E-09 OK| | CO2-Mass Fraction | 1.01 | 9.4E-02 | 2.1E+00 | 5.3 1.3E-10 OK| | H2O-Mass Fraction | 1.01 | 9.4E-02 | 2.1E+00 | 5.3 1.3E-10 OK| +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt | K-TurbKE | 0.99 | 7.7E-03 | 5.0E-02 | 5.4 3.6E-09 OK| | E-Diss.K | 0.97 | 5.0E-03 | 5.7E-02 | 12.0 1.1E-16 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.96 | 1.9E-02 | 4.2E-01 | 5.4 2.8E-10 OK| | O2-Mass Fraction | 1.00 | 4.3E-02 | 2.4E-01 | 5.4 1.7E-09 OK| | CO2-Mass Fraction | 1.00 | 9.6E-02 | 2.1E+00 | 5.4 1.2E-10 OK| | H2O-Mass Fraction | 1.00 | 9.6E-02 | 2.1E+00 | 5.4 1.2E-10 OK| +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt | V-Mom | 1.00 | 1.1E-02 | 7.1E-02 | 1.2E-03 OK| | W-Mom | 1.03 | 3.2E-03 | 1.9E-02 | 4.5E-03 OK| | P-Mass | 0.98 | 1.2E-05 | 7.2E-05 | 8.5 4.2E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 1.00 | 3.9E-02 | 2.0E-01 | 5.4 1.3E-09 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.99 | 7.5E-03 | 4.7E-02 | 5.4 2.6E-09 OK| | E-Diss.K | 0.98 | 4.7E-03 | 5.2E-02 | 12.0 7.9E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.97 | 1.8E-02 | 3.7E-01 | 5.4 2.3E-10 OK| | O2-Mass Fraction | 1.00 | 4.2E-02 | 2.4E-01 | 5.4 1.3E-09 OK| | CO2-Mass Fraction | 0.97 | 9.0E-02 | 1.7E+00 | 5.4 1.1E-10 OK| | H2O-Mass Fraction | 0.97 | 9.0E-02 | 1.7E+00 | 5.4 1.1E-10 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 54 CPU SECONDS = 5.136E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 1.01 | 1.5E-03 | 1.1E-02 | 7.5E-03 OK| | V-Mom | 1.00 | 1.1E-02 | 7.2E-02 | 1.2E-03 OK| | W-Mom | 1.03 | 3.4E-03 | 2.1E-02 | 4.6E-03 OK| | P-Mass | 0.98 | 1.2E-05 | 7.1E-05 | 8.5 4.4E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 1.00 | 3.9E-02 | 2.0E-01 | 5.4 9.5E-10 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 0.99 | 7.5E-03 | 4.6E-02 | 5.3 2.1E-09 OK| | E-Diss.K | 0.98 | 4.5E-03 | 4.9E-02 | 12.0 8.3E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.97 | 1.7E-02 | 3.4E-01 | 5.4 2.0E-10 OK| | O2-Mass Fraction | 1.00 | 4.2E-02 | 2.4E-01 | 5.4 9.3E-10 OK| | CO2-Mass Fraction | 0.98 | 8.6E-02 | 1.5E+00 | 5.4 9.3E-11 OK|

coffee husk outfiles.txt | H2O-Mass Fraction | 0.98 | 8.6E-02 | 1.5E+00 | 5.4 9.3E-11 OK| +----------------------+------+---------+---------+------------------+

======================================================================Page 45

coffee husk outfiles.txt OUTER LOOP ITERATION = 56 CPU SECONDS = 5.325E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 1.01 | 1.5E-03 | 1.1E-02 | 7.7E-03 OK| | V-Mom | 1.00 | 1.1E-02 | 7.3E-02 | 1.2E-03 OK| | W-Mom | 1.03 | 3.6E-03 | 2.2E-02 | 4.8E-03 OK| | P-Mass | 0.99 | 1.1E-05 | 6.9E-05 | 8.5 4.6E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 1.00 | 3.9E-02 | 2.0E-01 | 5.3 7.8E-10 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 7.4E-03 | 4.4E-02 | 5.4 1.8E-09 OK| | E-Diss.K | 0.99 | 4.4E-03 | 4.5E-02 | 12.0 7.2E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 1.00 | 1.6E-02 | 3.2E-01 | 5.3 1.7E-10 OK| | O2-Mass Fraction | 1.00 | 4.2E-02 | 2.3E-01 | 5.3 7.6E-10 OK| | CO2-Mass Fraction | 0.98 | 8.2E-02 | 1.3E+00 | 5.3 9.3E-11 OK| | H2O-Mass Fraction | 0.98 | 8.2E-02 | 1.3E+00 | 5.3 9.3E-11 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 58 CPU SECONDS = 5.517E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 1.00 | 1.6E-03 | 1.1E-02 | 7.9E-03 OK| | V-Mom | 1.00 | 1.1E-02 | 7.2E-02 | 1.2E-03 OK| | W-Mom | 1.02 | 3.8E-03 | 2.3E-02 | 4.9E-03 OK| | P-Mass | 0.99 | 1.1E-05 | 6.7E-05 | 8.5 4.7E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 1.00 | 3.8E-02 | 1.9E-01 | 5.4 5.5E-10 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 7.3E-03 | 4.2E-02 | 5.3 1.6E-09 OK|

coffee husk outfiles.txt | E-Diss.K | 0.99 | 4.3E-03 | 4.2E-02 | 12.0 8.0E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.98 | 1.5E-02 | 3.0E-01 | 5.4 1.4E-10 OK| | O2-Mass Fraction | 1.00 | 4.1E-02 | 2.3E-01 | 5.4 5.4E-10 OK| | CO2-Mass Fraction | 0.98 | 7.9E-02 | 1.2E+00 | 5.4 8.8E-11 OK| | H2O-Mass Fraction | 0.98 | 7.9E-02 | 1.2E+00 | 5.4 8.8E-11 OK| +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt | W-Mom | 1.02 | 4.0E-03 | 2.5E-02 | 5.0E-03 OK| | P-Mass | 0.99 | 1.1E-05 | 6.3E-05 | 8.5 5.0E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 1.00 | 3.8E-02 | 1.8E-01 | 5.3 4.0E-10 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 7.2E-03 | 4.1E-02 | 5.3 1.3E-09 OK| | E-Diss.K | 0.99 | 4.2E-03 | 3.7E-02 | 12.0 9.4E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.98 | 1.4E-02 | 2.8E-01 | 5.3 1.1E-10 OK| | O2-Mass Fraction | 1.00 | 4.1E-02 | 2.2E-01 | 5.3 3.9E-10 OK| | CO2-Mass Fraction | 0.98 | 7.4E-02 | 1.0E+00 | 5.3 7.0E-11 OK| | H2O-Mass Fraction | 0.98 | 7.4E-02 | 1.0E+00 | 5.3 7.0E-11 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 62 CPU SECONDS = 5.895E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 1.00 | 1.6E-03 | 1.1E-02 | 8.2E-03 OK| | V-Mom | 1.00 | 1.0E-02 | 7.2E-02 | 1.2E-03 OK| | W-Mom | 1.02 | 4.1E-03 | 2.6E-02 | 5.0E-03 OK| | P-Mass | 0.99 | 1.1E-05 | 6.2E-05 | 8.5 5.0E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 1.00 | 3.7E-02 | 1.8E-01 | 5.3 3.6E-10 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 7.2E-03 | 4.1E-02 | 5.3 1.3E-09 OK| | E-Diss.K | 0.99 | 4.1E-03 | 3.6E-02 | 12.0 8.5E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.98 | 1.4E-02 | 2.7E-01 | 5.3 1.0E-10 OK| | O2-Mass Fraction | 1.00 | 4.1E-02 | 2.2E-01 | 5.3 3.5E-10 OK| | CO2-Mass Fraction | 0.99 | 7.3E-02 | 9.8E-01 | 5.3 6.7E-11 OK| | H2O-Mass Fraction | 0.99 | 7.3E-02 | 9.8E-01 | 5.3 6.7E-11 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 63 CPU SECONDS = 5.988E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 1.00 | 1.6E-03 | 1.1E-02 | 8.3E-03 OK| | V-Mom | 1.00 | 1.0E-02 | 7.1E-02 | 1.2E-03 OK| | W-Mom | 1.02 | 4.1E-03 | 2.6E-02 | 5.1E-03 OK| | P-Mass | 0.99 | 1.0E-05 | 6.1E-05 | 8.5 5.1E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 3.7E-02 | 1.8E-01 | 5.4 3.5E-10 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 7.2E-03 | 4.1E-02 | 5.3 1.1E-09 OK| | E-Diss.K | 0.99 | 4.1E-03 | 3.6E-02 | 12.0 8.3E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.98 | 1.4E-02 | 2.6E-01 | 5.4 9.6E-11 OK| | O2-Mass Fraction | 1.00 | 4.1E-02 | 2.2E-01 | 5.4 3.4E-10 OK| | CO2-Mass Fraction | 0.99 | 7.3E-02 | 9.5E-01 | 5.4 6.1E-11 OK| | H2O-Mass Fraction | 0.99 | 7.3E-02 | 9.5E-01 | 5.4 6.1E-11 OK|

====================================================================== OUTER LOOP ITERATION = 67 CPU SECONDS = 6.364E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 1.00 | 1.6E-03 | 1.2E-02 | 8.6E-03 OK| | V-Mom | 1.00 | 1.0E-02 | 6.9E-02 | 1.2E-03 OK| | W-Mom | 1.01 | 4.3E-03 | 2.9E-02 | 5.2E-03 OK| | P-Mass | 0.99 | 1.0E-05 | 6.2E-05 | 8.5 5.3E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 3.7E-02 | 1.7E-01 | 5.3 2.2E-10 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 7.1E-03 | 4.2E-02 | 5.3 8.8E-10 OK| | E-Diss.K | 0.99 | 4.0E-03 | 3.3E-02 | 12.0 6.6E-17 OK|

coffee husk outfiles.txt +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.98 | 1.3E-02 | 2.4E-01 | 5.3 7.3E-11 OK| | O2-Mass Fraction | 1.00 | 4.0E-02 | 2.1E-01 | 5.3 2.1E-10 OK| | CO2-Mass Fraction | 1.00 | 7.1E-02 | 8.6E-01 | 5.3 4.9E-11 OK| | H2O-Mass Fraction | 1.00 | 7.1E-02 | 8.6E-01 | 5.3 4.9E-11 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 70 CPU SECONDS = 6.647E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 0.99 | 1.5E-03 | 1.1E-02 | 8.7E-03 OK| | V-Mom | 0.99 | 1.0E-02 | 6.6E-02 | 1.2E-03 OK| | W-Mom | 1.01 | 4.4E-03 | 3.0E-02 | 5.3E-03 OK|

coffee husk outfiles.txt | P-Mass | 0.99 | 9.7E-06 | 6.0E-05 | 8.5 5.5E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 3.6E-02 | 1.7E-01 | 5.3 1.7E-10 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 7.1E-03 | 4.3E-02 | 5.3 7.4E-10 OK| | E-Diss.K | 0.99 | 3.9E-03 | 3.0E-02 | 12.0 9.8E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.99 | 1.2E-02 | 2.2E-01 | 5.3 6.3E-11 OK| | O2-Mass Fraction | 1.00 | 4.0E-02 | 2.2E-01 | 5.3 1.6E-10 OK| | CO2-Mass Fraction | 1.00 | 7.1E-02 | 8.4E-01 | 5.3 4.9E-11 OK| | H2O-Mass Fraction | 1.00 | 7.1E-02 | 8.4E-01 | 5.3 4.9E-11 OK| +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 7.0E-03 | 4.5E-02 | 5.3 5.2E-10 OK| | E-Diss.K | 1.00 | 3.8E-03 | 2.9E-02 | 12.0 8.0E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.99 | 1.2E-02 | 2.0E-01 | 5.3 4.3E-11 OK| | O2-Mass Fraction | 1.00 | 3.9E-02 | 2.1E-01 | 5.3 8.5E-11 OK| | CO2-Mass Fraction | 0.98 | 6.6E-02 | 7.7E-01 | 5.3 3.6E-11 OK| | H2O-Mass Fraction | 0.98 | 6.6E-02 | 7.7E-01 | 5.3 3.6E-11 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 76 CPU SECONDS = 7.208E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 0.99 | 1.5E-03 | 1.1E-02 | 9.0E-03 OK| | V-Mom | 0.99 | 1.0E-02 | 6.9E-02 | 1.1E-03 OK| | W-Mom | 1.00 | 4.5E-03 | 3.2E-02 | 5.4E-03 OK| | P-Mass | 0.99 | 9.1E-06 | 5.4E-05 | 8.5 5.8E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 3.5E-02 | 1.7E-01 | 5.3 8.9E-11 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 7.0E-03 | 4.5E-02 | 5.3 4.8E-10 OK| | E-Diss.K | 1.00 | 3.8E-03 | 2.9E-02 | 12.0 6.8E-17 OK| +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt | Fuel Gas-Mass Fracti | 0.99 | 1.2E-02 | 2.0E-01 | 5.3 4.2E-11 OK| | O2-Mass Fraction | 1.00 | 3.9E-02 | 2.1E-01 | 5.3 8.2E-11 OK| | CO2-Mass Fraction | 0.99 | 6.5E-02 | 7.6E-01 | 5.3 3.5E-11 OK| | H2O-Mass Fraction | 0.99 | 6.5E-02 | 7.6E-01 | 5.3 3.5E-11 OK| +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 3.4E-02 | 1.7E-01 | 5.3 6.7E-11 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 6.9E-03 | 4.6E-02 | 5.3 4.1E-10 OK| | E-Diss.K | 1.00 | 3.8E-03 | 3.0E-02 | 12.0 8.1E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.99 | 1.1E-02 | 1.9E-01 | 5.3 3.6E-11 OK| | O2-Mass Fraction | 1.00 | 3.9E-02 | 2.1E-01 | 5.3 6.2E-11 OK| | CO2-Mass Fraction | 0.99 | 6.3E-02 | 7.2E-01 | 5.3 3.0E-11 OK| | H2O-Mass Fraction | 0.99 | 6.3E-02 | 7.2E-01 | 5.3 3.0E-11 OK| +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt ====================================================================== OUTER LOOP ITERATION = 82 CPU SECONDS = 7.770E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 0.99 | 1.4E-03 | 1.1E-02 | 9.2E-03 OK| | V-Mom | 0.99 | 9.6E-03 | 6.8E-02 | 1.1E-03 OK| | W-Mom | 1.00 | 4.5E-03 | 3.3E-02 | 5.5E-03 OK| | P-Mass | 0.99 | 8.5E-06 | 5.2E-05 | 8.5 6.1E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 3.4E-02 | 1.6E-01 | 5.3 5.8E-11 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 6.9E-03 | 4.7E-02 | 5.3 3.7E-10 OK| | E-Diss.K | 1.00 | 3.7E-03 | 3.1E-02 | 12.0 6.7E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.99 | 1.1E-02 | 1.8E-01 | 5.3 2.9E-11 OK| | O2-Mass Fraction | 1.00 | 3.8E-02 | 2.0E-01 | 5.3 5.3E-11 OK| | CO2-Mass Fraction | 0.99 | 6.0E-02 | 6.7E-01 | 5.3 3.1E-11 OK| | H2O-Mass Fraction | 0.99 | 6.0E-02 | 6.7E-01 | 5.3 3.1E-11 OK| +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt | K-TurbKE | 1.00 | 6.9E-03 | 4.8E-02 | 5.3 3.3E-10 OK| | E-Diss.K | 1.00 | 3.7E-03 | 3.1E-02 | 12.0 6.6E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.99 | 1.1E-02 | 1.7E-01 | 5.3 2.6E-11 OK| | O2-Mass Fraction | 1.00 | 3.8E-02 | 1.9E-01 | 5.3 5.1E-11 OK| | CO2-Mass Fraction | 0.99 | 5.9E-02 | 6.3E-01 | 5.3 3.2E-11 OK| | H2O-Mass Fraction | 0.99 | 5.9E-02 | 6.3E-01 | 5.3 3.2E-11 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 88 CPU SECONDS = 8.333E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 1.00 | 1.3E-03 | 1.2E-02 | 9.3E-03 OK| | V-Mom | 1.00 | 9.4E-03 | 6.3E-02 | 1.1E-03 OK| | W-Mom | 1.00 | 4.4E-03 | 3.2E-02 | 5.6E-03 OK| | P-Mass | 0.99 | 8.0E-06 | 5.1E-05 | 8.5 6.4E-02 OK| +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 3.2E-02 | 1.4E-01 | 5.4 4.3E-11 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 6.8E-03 | 4.8E-02 | 5.3 2.8E-10 OK| | E-Diss.K | 1.00 | 3.7E-03 | 3.1E-02 | 12.0 7.0E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.99 | 1.0E-02 | 1.6E-01 | 5.4 2.1E-11 OK| | O2-Mass Fraction | 1.00 | 3.8E-02 | 1.9E-01 | 5.4 3.8E-11 OK| | CO2-Mass Fraction | 0.99 | 5.5E-02 | 5.4E-01 | 5.4 2.8E-11 OK| | H2O-Mass Fraction | 0.99 | 5.5E-02 | 5.4E-01 | 5.4 2.8E-11 OK| +----------------------+------+---------+---------+------------------+

======================================================================Page 60

coffee husk outfiles.txt OUTER LOOP ITERATION = 91 CPU SECONDS = 8.612E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 1.00 | 1.3E-03 | 1.3E-02 | 9.4E-03 OK| | V-Mom | 1.00 | 9.2E-03 | 6.4E-02 | 1.1E-03 OK| | W-Mom | 1.00 | 4.4E-03 | 3.2E-02 | 5.5E-03 OK| | P-Mass | 0.99 | 7.8E-06 | 4.9E-05 | 8.5 6.5E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 3.2E-02 | 1.4E-01 | 5.4 3.9E-11 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 6.8E-03 | 4.8E-02 | 5.3 2.4E-10 OK| | E-Diss.K | 1.00 | 3.7E-03 | 3.1E-02 | 12.0 7.4E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.99 | 1.0E-02 | 1.6E-01 | 5.4 1.8E-11 OK| | O2-Mass Fraction | 1.00 | 3.7E-02 | 1.9E-01 | 5.4 3.3E-11 OK| | CO2-Mass Fraction | 0.99 | 5.3E-02 | 5.2E-01 | 5.4 3.3E-11 OK| | H2O-Mass Fraction | 0.99 | 5.3E-02 | 5.2E-01 | 5.4 3.3E-11 OK| +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt | E-Diss.K | 1.00 | 3.7E-03 | 3.2E-02 | 12.0 6.8E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.99 | 9.8E-03 | 1.5E-01 | 5.3 1.6E-11 OK| | O2-Mass Fraction | 1.00 | 3.7E-02 | 1.9E-01 | 5.3 3.0E-11 OK| | CO2-Mass Fraction | 0.99 | 5.2E-02 | 5.1E-01 | 5.3 3.4E-11 OK| | H2O-Mass Fraction | 0.99 | 5.2E-02 | 5.1E-01 | 5.3 3.4E-11 OK| +----------------------+------+---------+---------+------------------+

+--------------------------------------------------------------------+ | Particle Fate Diagnostics | +--------------------------------------------------------------------+

====================================================================== OUTER LOOP ITERATION = 97 CPU SECONDS = 9.167E+01 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 1.00 | 1.3E-03 | 1.4E-02 | 9.5E-03 OK| | V-Mom | 1.00 | 9.0E-03 | 6.4E-02 | 1.0E-03 OK| | W-Mom | 1.00 | 4.3E-03 | 3.2E-02 | 5.5E-03 OK| | P-Mass | 0.99 | 7.4E-06 | 4.3E-05 | 8.5 6.8E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal |

coffee husk outfiles.txt | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 3.0E-02 | 1.4E-01 | 5.3 3.1E-11 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 6.7E-03 | 4.7E-02 | 5.3 2.2E-10 OK| | E-Diss.K | 1.00 | 3.7E-03 | 3.2E-02 | 12.0 7.2E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.99 | 9.5E-03 | 1.5E-01 | 5.3 1.4E-11 OK| | O2-Mass Fraction | 1.00 | 3.6E-02 | 1.9E-01 | 5.3 2.5E-11 OK| | CO2-Mass Fraction | 0.99 | 5.0E-02 | 4.7E-01 | 5.3 3.3E-11 OK| | H2O-Mass Fraction | 0.99 | 5.0E-02 | 4.7E-01 | 5.3 3.3E-11 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 100 CPU SECONDS = 9.450E+01

coffee husk outfiles.txt ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 1.00 | 1.3E-03 | 1.5E-02 | 9.5E-03 OK| | V-Mom | 1.00 | 8.9E-03 | 6.3E-02 | 1.0E-03 OK| | W-Mom | 1.00 | 4.3E-03 | 3.2E-02 | 5.4E-03 OK| | P-Mass | 0.99 | 7.2E-06 | 4.3E-05 | 8.5 6.9E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 3.0E-02 | 1.4E-01 | 5.3 3.0E-11 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 6.7E-03 | 4.6E-02 | 5.3 1.8E-10 OK| | E-Diss.K | 1.00 | 3.7E-03 | 3.2E-02 | 12.0 7.0E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.99 | 9.3E-03 | 1.4E-01 | 5.3 1.2E-11 OK| | O2-Mass Fraction | 1.00 | 3.6E-02 | 1.9E-01 | 5.3 2.4E-11 OK| | CO2-Mass Fraction | 0.99 | 4.8E-02 | 4.5E-01 | 5.3 2.9E-11 OK| | H2O-Mass Fraction | 0.99 | 4.8E-02 | 4.5E-01 | 5.3 2.9E-11 OK| +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 2.8E-02 | 1.3E-01 | 5.3 1.9E-11 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 6.6E-03 | 4.4E-02 | 5.3 1.4E-10 OK| | E-Diss.K | 1.00 | 3.7E-03 | 3.1E-02 | 12.0 7.2E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.99 | 8.9E-03 | 1.3E-01 | 5.3 9.4E-12 OK| | O2-Mass Fraction | 1.00 | 3.5E-02 | 1.9E-01 | 5.3 1.6E-11 OK| | CO2-Mass Fraction | 0.99 | 4.6E-02 | 4.2E-01 | 5.3 2.9E-11 OK| | H2O-Mass Fraction | 0.99 | 4.6E-02 | 4.2E-01 | 5.3 2.9E-11 OK| +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 1.00 | 1.4E-03 | 1.6E-02 | 9.7E-03 OK| | V-Mom | 1.00 | 8.5E-03 | 6.7E-02 | 1.0E-03 OK| | W-Mom | 1.00 | 4.1E-03 | 3.1E-02 | 5.3E-03 OK| | P-Mass | 0.99 | 6.8E-06 | 4.3E-05 | 8.5 7.4E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 2.8E-02 | 1.3E-01 | 5.3 1.7E-11 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 6.6E-03 | 4.3E-02 | 5.3 1.6E-10 OK| | E-Diss.K | 1.00 | 3.7E-03 | 3.1E-02 | 12.0 8.4E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.99 | 8.7E-03 | 1.3E-01 | 5.3 7.2E-12 OK| | O2-Mass Fraction | 1.00 | 3.5E-02 | 1.8E-01 | 5.3 1.2E-11 OK| | CO2-Mass Fraction | 0.99 | 4.5E-02 | 4.2E-01 | 5.3 4.0E-11 OK| | H2O-Mass Fraction | 0.99 | 4.5E-02 | 4.2E-01 | 5.3 4.0E-11 OK| +----------------------+------+---------+---------+------------------+

+--------------------------------------------------------------------+ | Particle Equation | Total source and source change rates | +--------------------------------------------------------------------+ | | Equation Source Rate | +--------------------------------------------------------------------+ | Domain: reactor | +--------------------------------------------------------------------+ | Coffee Husk | Mass-Fuel Gas 2.962E-08 0.0000 | +--------------------------------------------------------------------+ | Coffee Husk | Mass-O2 1.252E-38 0.0000 | +--------------------------------------------------------------------+

coffee husk outfiles.txt +----------------------+------+---------+---------+------------------+ | U-Mom | 1.00 | 1.4E-03 | 1.6E-02 | 1.0E-02 OK| | V-Mom | 1.00 | 8.2E-03 | 6.5E-02 | 1.0E-03 OK| | W-Mom | 1.00 | 4.0E-03 | 3.0E-02 | 5.2E-03 OK| | P-Mass | 0.99 | 6.3E-06 | 3.5E-05 | 8.5 8.0E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 2.6E-02 | 1.2E-01 | 5.3 1.2E-11 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 6.5E-03 | 4.0E-02 | 5.3 1.2E-10 OK| | E-Diss.K | 1.00 | 3.8E-03 | 3.0E-02 | 12.0 8.0E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.99 | 8.1E-03 | 1.2E-01 | 5.3 5.9E-12 OK| | O2-Mass Fraction | 1.00 | 3.4E-02 | 1.8E-01 | 5.3 8.7E-12 OK| | CO2-Mass Fraction | 0.99 | 4.2E-02 | 4.1E-01 | 5.3 3.4E-11 OK| | H2O-Mass Fraction | 0.99 | 4.2E-02 | 4.1E-01 | 5.3 3.4E-11 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 120 CPU SECONDS = 1.130E+02 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 1.00 | 1.4E-03 | 1.6E-02 | 1.0E-02 OK| | V-Mom | 1.00 | 8.2E-03 | 6.4E-02 | 1.0E-03 OK| | W-Mom | 1.00 | 4.0E-03 | 3.0E-02 | 5.2E-03 OK| | P-Mass | 0.99 | 6.2E-06 | 3.4E-05 | 8.5 8.2E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 2.6E-02 | 1.2E-01 | 5.3 1.3E-11 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 6.5E-03 | 3.9E-02 | 5.3 1.1E-10 OK| | E-Diss.K | 1.00 | 3.9E-03 | 3.0E-02 | 12.0 8.1E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.99 | 8.0E-03 | 1.2E-01 | 5.3 6.1E-12 OK|

coffee husk outfiles.txt | O2-Mass Fraction | 1.00 | 3.4E-02 | 1.8E-01 | 5.3 8.8E-12 OK| | CO2-Mass Fraction | 0.99 | 4.1E-02 | 3.8E-01 | 5.3 4.0E-11 OK| | H2O-Mass Fraction | 0.99 | 4.1E-02 | 3.8E-01 | 5.3 4.0E-11 OK| +----------------------+------+---------+---------+------------------+

======================================================================Page 75

coffee husk outfiles.txt Particle Diagnostics ======================================================================

coffee husk outfiles.txt | U-Mom | 1.00 | 1.4E-03 | 1.7E-02 | 1.0E-02 OK| | V-Mom | 1.00 | 7.9E-03 | 6.2E-02 | 1.1E-03 OK| | W-Mom | 1.00 | 3.9E-03 | 2.9E-02 | 5.3E-03 OK| | P-Mass | 0.99 | 5.9E-06 | 3.5E-05 | 8.5 8.7E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 2.5E-02 | 1.2E-01 | 5.3 1.0E-11 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 6.5E-03 | 3.9E-02 | 5.3 1.0E-10 OK| | E-Diss.K | 1.01 | 4.0E-03 | 3.2E-02 | 12.0 7.1E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.99 | 7.6E-03 | 1.1E-01 | 5.3 4.4E-12 OK| | O2-Mass Fraction | 1.00 | 3.4E-02 | 1.9E-01 | 5.3 7.2E-12 OK| | CO2-Mass Fraction | 0.99 | 3.9E-02 | 3.6E-01 | 5.3 5.4E-11 OK| | H2O-Mass Fraction | 0.99 | 3.9E-02 | 3.6E-01 | 5.3 5.4E-11 OK| +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt | CO2-Mass Fraction | 0.99 | 3.8E-02 | 3.6E-01 | 5.3 6.0E-11 OK| | H2O-Mass Fraction | 0.99 | 3.8E-02 | 3.6E-01 | 5.3 6.0E-11 OK| +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt | V-Mom | 1.00 | 7.6E-03 | 6.3E-02 | 1.1E-03 OK| | W-Mom | 1.00 | 3.8E-03 | 2.9E-02 | 5.3E-03 OK| | P-Mass | 0.99 | 5.5E-06 | 3.2E-05 | 8.5 9.3E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 2.4E-02 | 1.2E-01 | 5.3 7.9E-12 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 6.4E-03 | 3.9E-02 | 5.3 7.9E-11 OK| | E-Diss.K | 1.01 | 4.2E-03 | 3.6E-02 | 12.0 7.3E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.99 | 7.2E-03 | 1.0E-01 | 5.3 4.5E-12 OK| | O2-Mass Fraction | 1.00 | 3.3E-02 | 1.8E-01 | 5.3 5.5E-12 OK| | CO2-Mass Fraction | 0.99 | 3.6E-02 | 3.4E-01 | 5.3 6.2E-11 OK| | H2O-Mass Fraction | 0.99 | 3.6E-02 | 3.4E-01 | 5.3 6.2E-11 OK| +----------------------+------+---------+---------+------------------+

====================================================================== OUTER LOOP ITERATION = 138 CPU SECONDS = 1.298E+02 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 1.00 | 1.4E-03 | 1.7E-02 | 1.1E-02 OK| | V-Mom | 1.00 | 7.6E-03 | 6.2E-02 | 1.1E-03 OK| | W-Mom | 1.00 | 3.8E-03 | 2.9E-02 | 5.3E-03 OK| | P-Mass | 0.99 | 5.5E-06 | 3.1E-05 | 8.5 9.5E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.01 | +----------------------+------+---------+---------+------------------+ | H-Energy | 0.99 | 2.3E-02 | 1.2E-01 | 5.3 7.5E-12 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 6.4E-03 | 3.9E-02 | 5.3 8.7E-11 OK| | E-Diss.K | 1.01 | 4.3E-03 | 3.7E-02 | 12.0 8.0E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.99 | 7.1E-03 | 9.9E-02 | 5.3 4.5E-12 OK| | O2-Mass Fraction | 1.00 | 3.3E-02 | 1.8E-01 | 5.3 5.2E-12 OK| | CO2-Mass Fraction | 0.99 | 3.5E-02 | 3.3E-01 | 5.3 6.4E-11 OK|

coffee husk outfiles.txt | H2O-Mass Fraction | 0.99 | 3.5E-02 | 3.3E-01 | 5.3 6.4E-11 OK| +----------------------+------+---------+---------+------------------+

+--------------------------------------------------------------------+ | Particle Equation | Total source and source change rates | +--------------------------------------------------------------------+ | | Equation Source Rate | +--------------------------------------------------------------------+

coffee husk outfiles.txt | H-Energy | 0.99 | 2.2E-02 | 1.0E-01 | 5.3 6.3E-12 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 6.2E-03 | 3.9E-02 | 5.3 5.9E-11 OK| | E-Diss.K | 1.00 | 4.5E-03 | 4.1E-02 | 12.0 6.4E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.99 | 6.5E-03 | 8.8E-02 | 5.3 5.3E-12 OK| | O2-Mass Fraction | 1.00 | 3.2E-02 | 1.7E-01 | 5.3 5.4E-12 OK| | CO2-Mass Fraction | 0.99 | 3.2E-02 | 2.7E-01 | 5.3 7.1E-11 OK| | H2O-Mass Fraction | 0.99 | 3.2E-02 | 2.7E-01 | 5.3 7.1E-11 OK| +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt | W-Mom | 0.99 | 3.0E-03 | 2.6E-02 | 2.6E-03 OK| | P-Mass | 0.98 | 4.3E-06 | 2.6E-05 | 12.2 6.8E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.00 | +----------------------+------+---------+---------+------------------+ | H-Energy | 1.00 | 1.9E-02 | 7.9E-02 | 5.3 6.1E-12 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 5.7E-03 | 3.9E-02 | 5.3 2.8E-11 OK| | E-Diss.K | 1.00 | 4.7E-03 | 4.3E-02 | 12.0 7.1E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 0.99 | 5.4E-03 | 6.7E-02 | 5.3 1.3E-11 OK| | O2-Mass Fraction | 1.00 | 3.0E-02 | 1.5E-01 | 5.3 6.4E-12 OK| | CO2-Mass Fraction | 1.00 | 2.6E-02 | 1.8E-01 | 5.3 7.1E-11 OK| | H2O-Mass Fraction | 1.00 | 2.6E-02 | 1.8E-01 | 5.3 7.1E-11 OK| +----------------------+------+---------+---------+------------------+

coffee husk outfiles.txt +--------------------------------------------------------------------+ | Coffee Husk | Energy 1.370E-01 0.0000 | +--------------------------------------------------------------------+ | Coffee Husk | Rad. Intensity 1.688E-03 0.0223 | +--------------------------------------------------------------------+

+--------------------------------------------------------------------+ | Particle Fate Diagnostics |

======================================================================Page 112

coffee husk outfiles.txt ====================================================================== Particle Diagnostics ======================================================================

======================================================================Page 127

+--------------------------------------------------------------------+ | Particle Equation | Total source and source change rates | +--------------------------------------------------------------------+ | | Equation Source Rate |

coffee husk outfiles.txt +--------------------------------------------------------------------+

+--------------------------------------------------------------------+Page 158

======================================================================Page 164

+--------------------------------------------------------------------+ | Particle Equation | Total source and source change rates | +--------------------------------------------------------------------+ | | Equation Source Rate | +--------------------------------------------------------------------+ | Domain: reactor | +--------------------------------------------------------------------+ | Coffee Husk | Mass-Fuel Gas 2.962E-08 0.0000 | +--------------------------------------------------------------------+

======================================================================Page 179

+--------------------------------------------------------------------+ | Particle Equation | Total source and source change rates | +--------------------------------------------------------------------+

coffee husk outfiles.txt +--------------------------------------------------------------------+

coffee husk outfiles.txt | | Exceeded time limit : 200 | +--------------------------------------------------------------------+

coffee husk outfiles.txt +--------------------------------------------------------------------+ | Particle Fate Diagnostics | +--------------------------------------------------------------------+ | Particle type | Fate type Particles | +--------------------------------------------------------------------+ | Coffee Husk | Entered domain : 200 | | | Exceeded time limit : 200 | +--------------------------------------------------------------------+

======================================================================Page 216

+--------------------------------------------------------------------+ | Particle Equation | Total source and source change rates |

======================================================================Page 231

coffee husk outfiles.txt | Coffee Husk | Rad. Intensity 1.137E-03 0.0056 | +--------------------------------------------------------------------+

+--------------------------------------------------------------------+ | Particle Fate Diagnostics | +--------------------------------------------------------------------+ | Particle type | Fate type Particles | +--------------------------------------------------------------------+

+--------------------------------------------------------------------+ | Particle Equation | Total source and source change rates | +--------------------------------------------------------------------+ | | Equation Source Rate | +--------------------------------------------------------------------+ | Domain: reactor | +--------------------------------------------------------------------+ | Coffee Husk | Mass-Fuel Gas 2.962E-08 0.0000 | +--------------------------------------------------------------------+ | Coffee Husk | Mass-O2 1.252E-38 0.0000 | +--------------------------------------------------------------------+ | Coffee Husk | Mass-CO2 1.722E-38 0.0000 | +--------------------------------------------------------------------+

+--------------------------------------------------------------------+ | Particle Equation | Total source and source change rates | +--------------------------------------------------------------------+ | | Equation Source Rate | +--------------------------------------------------------------------+ | Domain: reactor | +--------------------------------------------------------------------+

======================================================================Page 268

+--------------------------------------------------------------------+Page 276

====================================================================== OUTER LOOP ITERATION = 600 CPU SECONDS = 5.659E+02 ---------------------------------------------------------------------- | Equation | Rate | RMS Res | Max Res | Linear Solution | +----------------------+------+---------+---------+------------------+ | U-Mom | 1.00 | 8.6E-04 | 7.6E-03 | 3.3E-03 OK| | V-Mom | 1.00 | 2.1E-03 | 1.4E-02 | 5.0E-04 OK| | W-Mom | 1.00 | 2.9E-03 | 3.0E-02 | 1.7E-03 OK| | P-Mass | 0.99 | 1.6E-06 | 2.0E-05 | 12.2 6.9E-02 OK| +----------------------+------+---------+---------+------------------+ | I-Radiation | #Its | Vol Chg | Sur Chg | %Lost %Imbal | | Gray | 1 | 0.0E+00 | 0.0E+00 | 0.00 0.04 | +----------------------+------+---------+---------+------------------+ | H-Energy | 1.00 | 3.3E-03 | 1.4E-02 | 5.3 5.6E-12 OK| +----------------------+------+---------+---------+------------------+ | K-TurbKE | 1.00 | 4.0E-03 | 3.3E-02 | 5.3 1.5E-11 OK| | E-Diss.K | 1.00 | 4.3E-03 | 4.9E-02 | 12.0 7.0E-17 OK| +----------------------+------+---------+---------+------------------+ | Fuel Gas-Mass Fracti | 1.00 | 8.3E-03 | 8.8E-02 | 5.3 9.3E-12 OK| | O2-Mass Fraction | 1.00 | 2.3E-02 | 9.9E-02 | 5.3 3.8E-12 OK| | CO2-Mass Fraction | 1.00 | 6.3E-03 | 4.8E-02 | 5.3 2.5E-11 OK| | H2O-Mass Fraction | 1.00 | 6.3E-03 | 4.8E-02 | 5.3 2.5E-11 OK| +----------------------+------+---------+---------+------------------+ CFD Solver finished: Wed Jun 20 17:07:17 2012 CFD Solver wall clock seconds: 5.7700E+02

====================================================================== Termination and Interrupt Condition Summary ====================================================================== CFD Solver: Run duration reached (Maximum number of outer iterations)

====================================================================== Boundary Flow and Total Source Term Summary ======================================================================

+--------------------------------------------------------------------+ | U-Mom | +--------------------------------------------------------------------+ Boundary : Coffee Husk inlet 1.6426E-08 Boundary : airinlet 1.2226E-07 Boundary : hopperwall 1.9345E-02 Boundary : outlet -2.7333E-06 Boundary : reactorwall -1.9343E-02 Particle Source : Coffee Husk 2.1928E-11 ----------- Domain Imbalance : -1.1147E-06

Domain Imbalance, in %: -0.0007 %

+--------------------------------------------------------------------+ | V-Mom | +--------------------------------------------------------------------+ Boundary : Coffee Husk inlet 3.0135E-07 Boundary : airinlet -1.6520E-01 Boundary : hopperwall -2.1394E-03 Boundary : outlet -1.8148E-03 Boundary : reactorwall -1.5980E-04 Domain Src (Pos) : reactor 1.6917E-01 Particle Source : Coffee Husk -2.2777E-07 ----------- Domain Imbalance : -1.4801E-04

+--------------------------------------------------------------------+ | W-Mom | +--------------------------------------------------------------------+ Boundary : Coffee Husk inlet 3.2604E-02 Boundary : airinlet 2.5548E-07 Boundary : hopperwall 1.6087E-04 Boundary : outlet -4.7799E-06 Boundary : reactorwall -3.2755E-02 Particle Source : Coffee Husk 1.3967E-11 ----------- Domain Imbalance : 4.4955E-06

Domain Imbalance, in %: 0.0027 %

+--------------------------------------------------------------------+ | P-Mass | +--------------------------------------------------------------------+ Boundary : airinlet 4.9000E-03 Boundary : outlet -4.8999E-03 Particle Source : Coffee Husk 2.9617E-08 ----------- Domain Imbalance : 1.5955E-07

+--------------------------------------------------------------------+ | I-Radiation | +--------------------------------------------------------------------+ Boundary : Coffee Husk inlet -9.8296E+00 Boundary : airinlet -4.1588E+02 Boundary : hopperwall -1.0362E+02 Boundary : outlet -1.0769E+01 Boundary : reactorwall 1.5134E+03 Domain Src (Neg) : reactor -9.7919E+02 Domain Src (Pos) : reactor 5.9064E+00 Particle Source : Coffee Husk -1.0847E-03 ----------- Global Imbalance : -7.2499E-13

Global Imbalance, in %: 0.0000 %

+--------------------------------------------------------------------+ | H-Energy | +--------------------------------------------------------------------+ Boundary : airinlet 1.3859E+03

coffee husk outfiles.txt Boundary : hopperwall -9.8772E+00 Boundary : outlet -2.6069E+03 Boundary : reactorwall 4.9643E+01 Domain Src (Neg) : reactor -5.7495E+00 Domain Src (Pos) : reactor 9.7903E+02 Particle Source : Coffee Husk -1.3695E-01 ----------- Domain Imbalance : -2.0809E+02

+--------------------------------------------------------------------+ | Fuel Gas-Mass Fraction | +--------------------------------------------------------------------+ Boundary : outlet 3.9483E-15 Domain Src (Neg) : reactor -3.7370E-09 Particle Source : Coffee Husk 2.9617E-08 ----------- Domain Imbalance : 2.5880E-08

+--------------------------------------------------------------------+ | O2-Mass Fraction | +--------------------------------------------------------------------+ Boundary : airinlet 1.1368E-03 Boundary : outlet -3.7136E-05 Domain Src (Neg) : reactor -4.8417E-09 Particle Source : Coffee Husk -1.2520E-38 ----------- Domain Imbalance : 1.0997E-03

+--------------------------------------------------------------------+ | CO2-Mass Fraction | +--------------------------------------------------------------------+ Boundary : outlet 1.0509E-13 Domain Src (Pos) : reactor 6.2885E-09 Particle Source : Coffee Husk 1.7215E-38 ----------- Domain Imbalance : 6.2886E-09

+--------------------------------------------------------------------+ | H2O-Mass Fraction | +--------------------------------------------------------------------+ Boundary : outlet 3.9137E-14 Domain Src (Pos) : reactor 2.3419E-09 ----------- Domain Imbalance : 2.3420E-09

====================================================================== Wall Force and Moment Summary ====================================================================== Notes: 1. Pressure integrals exclude the reference pressure. To include it, set the expert parameter 'include pref in forces = t'.

+--------------------------------------------------------------------+ | Pressure Force On Walls | +--------------------------------------------------------------------+ X-Comp. Y-Comp. Z-Comp.

Domain Group: reactor

hopperwall 2.0836E-02 -4.6069E-03 1.7390E-04 reactorwall -2.0838E-02 -5.2192E-05 -3.5290E-02 ----------- ----------- ----------- Domain Group Totals : -1.5188E-06 -4.6591E-03 -3.5116E-02

+--------------------------------------------------------------------+ | Viscous Force On Walls | +--------------------------------------------------------------------+ X-Comp. Y-Comp. Z-Comp.

hopperwall -4.7791E-08 -1.3485E-06 5.3916E-07 reactorwall 8.6773E-08 1.4657E-04 -1.9335E-07 ----------- ----------- ----------- Domain Group Totals : 3.8982E-08 1.4522E-04 3.4580E-07

+--------------------------------------------------------------------+ | Pressure Moment On Walls | +--------------------------------------------------------------------+ X-Comp. Y-Comp. Z-Comp.

hopperwall 6.6494E-04 1.5811E-03 -1.1450E-03 reactorwall -1.6272E-03 -7.7458E-07 9.6414E-04 ----------- ----------- ----------- Domain Group Totals : -9.6226E-04 1.5803E-03 -1.8083E-04

+--------------------------------------------------------------------+ | Viscous Moment On Walls | +--------------------------------------------------------------------+ X-Comp. Y-Comp. Z-Comp.

hopperwall 2.9953E-07 -3.9998E-08 -9.5683E-08 reactorwall -6.3638E-07 3.8264E-09 1.6110E-07 ----------- ----------- ----------- Domain Group Totals : -3.3685E-07 -3.6172E-08 6.5420E-08

+--------------------------------------------------------------------+ | Locations of Maximum Residuals | +--------------------------------------------------------------------+ | Equation | Node # | X | Y | Z | +--------------------------------------------------------------------+ | U-Mom | 1226 | 5.101E-02 | 8.960E-02 | 1.400E-01 | | V-Mom | 1690 | 1.753E-02 | 6.322E-02 | 1.333E-01 | | W-Mom | 1226 | 5.101E-02 | 8.960E-02 | 1.400E-01 | | P-Mass | 1111 | 2.693E-02 | 8.621E-02 | 1.328E-01 | | H-Energy | 2523 | 5.463E-02 | 4.681E-02 | 1.700E-01 |

coffee husk outfiles.txt | K-TurbKE | 2186 | 7.115E-02 | 4.770E-02 | 8.297E-02 | | E-Diss.K | 1653 | 7.705E-02 | 2.690E-02 | 7.304E-02 | | Fuel Gas-Mass Fracti | 90 | 7.232E-02 | 9.239E-03 | 2.000E-01 | | O2-Mass Fraction | 1195 | 4.532E-02 | 9.000E-02 | 1.533E-01 | | CO2-Mass Fraction | 2220 | 4.831E-02 | 7.634E-02 | 8.381E-02 | | H2O-Mass Fraction | 2220 | 4.831E-02 | 7.634E-02 | 8.381E-02 | +--------------------------------------------------------------------+

+--------------------------------------------------------------------+ | Peak Values of Residuals | +--------------------------------------------------------------------+ | Equation | Loop # | Peak Residual | Final Residual | +--------------------------------------------------------------------+ | U-Mom | 2 | 4.45570E-02 | 8.61925E-04 | | V-Mom | 1 | 1.35909E+00 | 2.10393E-03 | | W-Mom | 2 | 2.04136E-01 | 2.88675E-03 | | P-Mass | 1 | 2.32929E-02 | 1.59496E-06 | | H-Energy | 1 | 2.90567E-01 | 3.28707E-03 | | K-TurbKE | 2 | 2.30822E-01 | 4.03775E-03 | | E-Diss.K | 1 | 2.57801E+00 | 4.26101E-03 | | Fuel Gas-Mass Fracti | 26 | 3.18791E-01 | 8.32369E-03 | | O2-Mass Fraction | 1 | 2.93769E-01 | 2.32020E-02 | | CO2-Mass Fraction | 27 | 2.57686E-01 | 6.32628E-03 | | H2O-Mass Fraction | 27 | 2.57686E-01 | 6.32629E-03 | +--------------------------------------------------------------------+

+--------------------------------------------------------------------+ | Average Scale Information | +--------------------------------------------------------------------+

Domain Name : reactor Global Length = 3.3614E-01 Minimum Extent = 2.0000E-01 Maximum Extent = 1.2000E+00 Density = 5.4029E-01 Dynamic Viscosity = 1.7982E-05 Velocity = 2.8887E-01 Advection Time = 1.1636E+00 Reynolds Number = 2.9174E+03 Speed of Sound = 5.0701E+02 Mach Number = 5.6974E-04 Thermal Conductivity = 2.6032E-02 Specific Heat Capacity at Constant Pressure = 1.0751E+03 Specific Heat Capacity at Constant Volume = 7.8522E+02

coffee husk outfiles.txt Specific Heat Ratio = 1.3692E+00 Prandtl Number = 7.4266E-01 Temperature Range = 3.1166E+02 Total Extinction Coefficient = 1.0000E+00 Optical Thickness = 3.3614E-01

+--------------------------------------------------------------------+ | Variable Range Information | +--------------------------------------------------------------------+

Domain Name : reactor +--------------------------------------------------------------------+ | Variable Name | min | max | +--------------------------------------------------------------------+ | Density | 4.29E-01 | 7.16E-01 | | Specific Heat Capacity at Constant Pressure| 1.05E+03 | 1.12E+03 | | Dynamic Viscosity | 1.77E-05 | 1.80E-05 | | Thermal Conductivity | 2.59E-02 | 2.61E-02 | | Isothermal Compressibility | 9.87E-06 | 9.87E-06 | | Static Entropy | 7.28E+03 | 7.88E+03 | | N2.Density | 4.29E-01 | 7.05E-01 | | N2.Specific Heat Capacity at Constant Press| 1.06E+03 | 1.12E+03 | | N2.Dynamic Viscosity | 1.77E-05 | 1.77E-05 | | N2.Thermal Conductivity | 2.59E-02 | 2.59E-02 | | N2.Isothermal Compressibility | 9.87E-06 | 9.87E-06 | | N2.Static Enthalpy | 1.95E+05 | 5.33E+05 | | N2.Static Entropy | 7.34E+03 | 7.88E+03 | | Fuel Gas.Density | 3.16E-01 | 5.19E-01 | | Fuel Gas.Specific Heat Capacity at Constant| 2.21E+03 | 2.21E+03 | | Fuel Gas.Dynamic Viscosity | 1.11E-05 | 1.11E-05 | | Fuel Gas.Thermal Conductivity | 3.43E-02 | 3.43E-02 | | Fuel Gas.Isothermal Compressibility | 9.87E-06 | 9.87E-06 | | Fuel Gas.Static Enthalpy | -6.19E+06 | -5.50E+06 | | Fuel Gas.Static Entropy | 1.25E+04 | 1.36E+04 | | O2.Density | 4.90E-01 | 8.05E-01 | | O2.Specific Heat Capacity at Constant Press| 9.68E+02 | 1.05E+03 | | O2.Dynamic Viscosity | 1.92E-05 | 1.92E-05 | | O2.Thermal Conductivity | 2.66E-02 | 2.66E-02 | | O2.Isothermal Compressibility | 9.87E-06 | 9.87E-06 | | O2.Static Enthalpy | 1.76E+05 | 4.91E+05 | | O2.Static Entropy | 6.87E+03 | 7.37E+03 | | CO2.Density | 6.74E-01 | 1.11E+00 | | CO2.Specific Heat Capacity at Constant Pres| 1.00E+03 | 1.17E+03 | | CO2.Dynamic Viscosity | 1.49E-05 | 1.49E-05 | | CO2.Thermal Conductivity | 1.45E-02 | 1.45E-02 | | CO2.Isothermal Compressibility | 9.87E-06 | 9.87E-06 | | CO2.Static Enthalpy | -8.77E+06 | -8.43E+06 | | CO2.Static Entropy | 5.30E+03 | 5.84E+03 | | H2O.Density | 2.76E-01 | 4.53E-01 | | H2O.Specific Heat Capacity at Constant Pres| 1.95E+03 | 2.14E+03 | | H2O.Dynamic Viscosity | 9.40E-06 | 9.40E-06 | | H2O.Thermal Conductivity | 1.93E-02 | 1.93E-02 | | H2O.Isothermal Compressibility | 9.87E-06 | 9.87E-06 | | H2O.Static Enthalpy | -1.31E+07 | -1.24E+07 | | H2O.Static Entropy | 1.14E+04 | 1.24E+04 | | Total Absorption Coefficient | 1.00E+00 | 1.00E+00 | | Total Scattering Coefficient | 0.00E+00 | 0.00E+00 | | Radiation Intensity | 3.02E+02 | 7.35E+03 | | Velocity u | -6.98E-02 | 5.57E-02 | | Velocity v | -1.17E-01 | 3.84E-01 | | Velocity w | -8.70E-02 | 1.44E-01 | | Pressure | -5.36E+00 | 9.99E-04 | | Turbulence Kinetic Energy | 2.46E-04 | 3.54E-03 |

coffee husk outfiles.txt | Turbulence Eddy Dissipation | 1.88E-05 | 7.70E-03 | | Eddy Viscosity | 3.06E-05 | 1.80E-04 | | Temperature | 4.85E+02 | 7.96E+02 | | Static Enthalpy | 1.88E+05 | 5.33E+05 | | N2.Mass Fraction | 7.68E-01 | 9.94E-01 | | Fuel Gas.Conservative Mass Fraction | -1.50E-08 | 9.75E-04 | | Fuel Gas.Mass Fraction | 0.00E+00 | 9.75E-04 | | O2.Conservative Mass Fraction | 6.10E-03 | 2.32E-01 | | O2.Mass Fraction | 6.10E-03 | 2.32E-01 | | CO2.Conservative Mass Fraction | -1.84E-08 | 3.53E-05 | | CO2.Mass Fraction | 0.00E+00 | 3.53E-05 | | H2O.Conservative Mass Fraction | -6.86E-09 | 1.32E-05 | | H2O.Mass Fraction | 0.00E+00 | 1.32E-05 | | Coffee Husk.Averaged Volume Fraction | 0.00E+00 | 2.14E+00 | +--------------------------------------------------------------------+

+--------------------------------------------------------------------+ | Particle Mass Flow Summary | +--------------------------------------------------------------------+

Coffee Husk Coffee Husk inlet 3.4690E-03

+--------------------------------------------------------------------+ | Particle Energy Flow Summary | +--------------------------------------------------------------------+

Coffee Husk Coffee Husk inlet 1.9014E+02

+--------------------------------------------------------------------+ | CPU Requirements of Numerical Solution | +--------------------------------------------------------------------+

Subsystem Name Discretization Linear Solution (secs. %total) (secs. %total) ---------------------------------------------------------------------- Momentum and Mass 1.91E+02 33.7 % 2.50E+01 4.4 % Thermal Radiation 1.16E+01 2.1 % 2.14E+01 3.8 % Heat Transfer 3.96E+01 7.0 % 5.27E+00 0.9 % TurbKE and Diss.K 4.27E+01 7.5 % 1.55E+01 2.7 % Mass Fractions 7.36E+01 13.0 % 1.99E+01 3.5 % -------- ------- -------- ------ Subsystem Summary 3.58E+02 63.2 % 8.70E+01 15.3 %

Particle Tracking 2.44E+00 0.4 % Variable Updates 9.75E+01 17.2 % File Reading 1.56E-02 0.0 % File Writing 1.72E-01 0.0 % Miscellaneous 2.18E+01 3.8 % -------- Total 5.67E+02

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

Host computer: USER-E0D9062D4BPage 289

coffee husk outfiles.txt Job finished: Wed Jun 20 17:07:18 2012 Total CPU time: 5.673E+02 seconds or: ( 0: 0: 9: 27.328 ) ( Days: Hours: Minutes: Seconds )

Total wall clock time: 5.820E+02 seconds or: ( 0: 0: 9: 42.000 ) ( Days: Hours: Minutes: Seconds )

End of solution stage.

+--------------------------------------------------------------------+ | The results from this run of the ANSYS CFX Solver have been | | written to C:\Documents and Settings\User\Local | | Settings\Temp\coffee husk | | gasifier_2396_Working\dp0\CFX\CFX\Work1\Fluid Flow_001.res | +--------------------------------------------------------------------+

This run of the ANSYS CFX Solver has finished.

coffee husk outfiles.txt - notepad

hc fuel fraction

coffee husk outfiles

end refractive index

end dynamic viscosity

end thermal conductivity

particle wall interaction

end absorption coefficient

end scattering coefficient

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