- EMTD - Static variable in class nce.heattransfer.HT
-
- enableMoreVerbose() - Static method in class nce.error.NCELog
-
- enableOutput() - Static method in class nce.error.NCELog
-
- enableVerbose() - Static method in class nce.error.NCELog
-
- enableWarnings() - Static method in class nce.error.NCEErr
-
- EnclosedBody - Class in nce.heattransfer.radiation
-
Radiant heat transferred from body 1 enclosed into body 2, general case.
- EnclosedBody() - Constructor for class nce.heattransfer.radiation.EnclosedBody
-
- EnclosedBodySmall - Class in nce.heattransfer.radiation
-
Radiant heat transferred from body 1 enclosed into body 2, were
Area2 >> Area1, eg.
- EnclosedBodySmall() - Constructor for class nce.heattransfer.radiation.EnclosedBodySmall
-
- epsAbs - Static variable in class nce.math.NCEMath
-
- epsAbsF - Static variable in class nce.math.NCEMath
-
- epsAbsX - Static variable in class nce.math.NCEMath
-
- epsRel - Static variable in class nce.math.NCEMath
-
- epsRelX - Static variable in class nce.math.NCEMath
-
- Equipment - Class in nce.equipments
-
Base class for the definition of process equipments
- Equipment() - Constructor for class nce.equipments.Equipment
-
- ERR - Static variable in class nce.base.NCE
-
- ErrorStack - Class in nce.error
-
Stack of errors to be associated to a calculation model.
- ErrorStack() - Constructor for class nce.error.ErrorStack
-
- evalAcentricFactor(double) - Method in class nce.phprop.vaporpressure.VaporPressureLeeKesler
-
Use to evaluate acentric factor from reduced saturation pressure at
Tr=0.7
- evalActivityCoefficients(double, double[], double[]) - Method in class nce.vle.ExcGibbsEnWilson
-
- evalAllAverageValues() - Method in class nce.base.DomainDecomposition
-
On domain of 3 steps, sets mid step value to the average between
first and last step for all
variables
- evalAverageMoleMass() - Method in class nce.stream.Stream
-
High level driver, evaluates average mole mass of a single phase stream.
- evalAverageSurfaceTemperature() - Method in class nce.heattransfer.extendedsurfaces.FinRectangular
-
- evalAverageValue(String) - Method in class nce.base.DomainDecomposition
-
On domain of 3 steps, sets mid step value to the average
between first and last step
- evalAzeotropeTemperature() - Method in class nce.vle.VleSolver
-
Checks if an azeotrope exists and evaluates azeotropic temperature
- evalAzeotropeTemperature() - Method in class nce.vle.VleSolverGamma
-
- evalAzeotropeTemperature() - Method in class nce.vle.VleSolverRaoult
-
- evalAzeotropicPressure() - Method in class nce.vle.VleSolver
-
Checks if an azeotrope exists and evaluates azeotropic pressure
- evalAzeotropicPressure() - Method in class nce.vle.VleSolverGamma
-
- evalAzeotropicPressure() - Method in class nce.vle.VleSolverRaoult
-
- evalBubP() - Method in class nce.vle.VleSolver
-
Evaluation of bubble pressure
- evalBubP() - Method in class nce.vle.VleSolverGamma
-
- evalBubP() - Method in class nce.vle.VleSolverRaoult
-
- evalBubT() - Method in class nce.vle.VleSolver
-
Evaluation of bubble pressure
- evalBubT() - Method in class nce.vle.VleSolverGamma
-
- evalBubT() - Method in class nce.vle.VleSolverRaoult
-
- evalBulkVariableFromInOutAverageAtAllSteps(String, String, DomainDecomposition.GridDirection, double) - Method in class nce.base.DomainDecomposition
-
Evaluates the bulk variable on a stage by taking the average between inlet
and outlet values of another variable on the same stage, eg.
- evalCompressionPower(Stream, double, double) - Method in class nce.equipments.CentrifCompressor
-
Evaluates the power required to compress an ideal gas
- evalCompressionPower() - Method in class nce.equipments.CentrifPump
-
Evaluates the power required to compress a liquid
- evalCp(double) - Method in class nce.datasets.models.SpecHeatEqnDataSet
-
- evalCp(double) - Method in class nce.phprop.specificheat.SpecHeatDataSet
-
Evaluates specific heat by interpolation in a data set table.
- evalCp(double) - Method in class nce.phprop.specificheat.SpecHeatEqnFixed
-
- evalCp(double) - Method in class nce.phprop.specificheat.SpecHeatEqnPoly2
-
- evalCp(double) - Method in class nce.phprop.specificheat.SpecHeatEqnPoly5
-
- evalCp(double) - Method in class nce.phprop.specificheat.SpecHeatEqnTrig
-
- evalCp(double) - Method in class nce.phprop.specificheat.SpecHeatMixRuleIdeal
-
- evalCp(double) - Method in class nce.phprop.specificheat.SpecHeatMixRuleIdealMass
-
- evalCp(double) - Method in class nce.phprop.specificheat.SpecHeatModel
-
returns specific heat at constant pressure as function of T
- evalCpIntH(double, double) - Method in class nce.datasets.models.SpecHeatEqnDataSet
-
- evalCpIntH(double, double) - Method in class nce.phprop.specificheat.SpecHeatDataSet
-
- evalCpIntH(double, double) - Method in class nce.phprop.specificheat.SpecHeatEqnFixed
-
- evalCpIntH(double, double) - Method in class nce.phprop.specificheat.SpecHeatEqnPoly2
-
- evalCpIntH(double, double) - Method in class nce.phprop.specificheat.SpecHeatEqnPoly5
-
- evalCpIntH(double, double) - Method in class nce.phprop.specificheat.SpecHeatEqnTrig
-
- evalCpIntH(double, double) - Method in class nce.phprop.specificheat.SpecHeatMixRuleIdeal
-
- evalCpIntH(double, double) - Method in class nce.phprop.specificheat.SpecHeatModel
-
Estimates the integral int_T0^T(Cp dT) / (T - T0), that can be used to
simplify enthalpy calculations.
- evalCpIntS(double, double) - Method in class nce.datasets.models.SpecHeatEqnDataSet
-
- evalCpIntS(double, double) - Method in class nce.phprop.specificheat.SpecHeatEqnFixed
-
- evalCpIntS(double, double) - Method in class nce.phprop.specificheat.SpecHeatEqnPoly2
-
- evalCpIntS(double, double) - Method in class nce.phprop.specificheat.SpecHeatEqnPoly5
-
- evalCpIntS(double, double) - Method in class nce.phprop.specificheat.SpecHeatEqnTrig
-
- evalCpIntS(double, double) - Method in class nce.phprop.specificheat.SpecHeatMixRuleIdeal
-
- evalCpIntS(double, double) - Method in class nce.phprop.specificheat.SpecHeatModel
-
- evalDensity(double, double) - Method in class nce.base.ChemicalSpecies
-
Evaluates species density using the model specified in 'activeDensityModel'
variable, taking into account also the physical state (liquid or vapor).
- evalDensity(double) - Method in class nce.databank.Material
-
- evalDensity(double, double) - Method in class nce.phprop.density.DensityDataSet
-
Evaluates mass density by interpolation in a data set table
- evalDensity(double, double) - Method in class nce.phprop.density.DensityEqnFixed
-
- evalDensity(double, double) - Method in class nce.phprop.density.DensityEqnPow
-
- evalDensity(double, double) - Method in class nce.phprop.density.DensityMixRuleIdealLiquid
-
- evalDensity(double, double) - Method in class nce.phprop.density.DensityModel
-
- evalDensity() - Method in class nce.phprop.eosgas.GasEosIdeal
-
Evaluates mass density
- evalDensity(double, double) - Method in class nce.phprop.molvolume.LiqMolVolModel
-
Evaluates liquid density as 1/volume, where volume is evaluated with
a user defined model
- evalDensity(double, double) - Method in class nce.stream.Stream
-
High level driver, evaluates stream sDensity [kg/m3].
- evalDensity(double, double) - Method in class nce.stream.StreamLiq
-
- evalDensity(double, double) - Method in class nce.stream.StreamVapLiq
-
Evaluates the density of a vapor/liquid mixture by mass averaging
- evalDensityMolar() - Method in class nce.phprop.eosgas.GasEosIdeal
-
evaluates molar density
- evalDensitySat(double, double) - Method in class nce.phprop.molvolume.LiqMolVolModel
-
Evaluates liquid density at saturation as 1/volume, where volume is
evaluated with a user defined model
- evalDewP() - Method in class nce.vle.VleSolver
-
Evaluation of dew pressure
- evalDewP() - Method in class nce.vle.VleSolverGamma
-
- evalDewP() - Method in class nce.vle.VleSolverRaoult
-
- evalDewT() - Method in class nce.vle.VleSolver
-
Evaluation of dew temperature
- evalDewT() - Method in class nce.vle.VleSolverGamma
-
- evalDewT() - Method in class nce.vle.VleSolverRaoult
-
- evalDHfromDT(double, double) - Method in class nce.stream.Stream
-
Evaluates enthalpy change associated to a certain temperature difference
- evalDTfromDH(double, double) - Method in class nce.stream.Stream
-
Back-calculates temperature variation from enthalpy change, using
the available model for integral specific heat
- evalEfficiency() - Method in class nce.heattransfer.extendedsurfaces.FinRectangular
-
- evalFilmCoeffAtAllSteps() - Method in class nce.equipments.doublepipe.HeatExchangerDoublePipeShellSide
-
- evalFilmCoeffAtAllSteps() - Method in class nce.equipments.doublepipe.HeatExchangerDoublePipeTubeSide
-
- evalFilmCoeffAtAllSteps() - Method in class nce.equipments.HeatExchangerSide
-
Evaluate film coefficient using one of the available correlations in
nce.heattransfer and the physical properties in the calculation grid.
- evalFilmCoefficient() - Method in class nce.equipments.HeatExchangerSide
-
Calculates the average film coefficient along computation domain
- evalFlowArea(Object) - Method in class nce.equipments.doublepipe.HeatExchangerDoublePipeShellSide
-
- evalFlowArea(Object) - Method in class nce.equipments.doublepipe.HeatExchangerDoublePipeTubeSide
-
- evalFlowArea(Object) - Method in class nce.equipments.HeatExchangerSide
-
- evalFricFacFanningChurchill(double, double) - Static method in class nce.piping.Pipe
-
Evaluates Fanning's friction factor with Churchill's equation.
- evalFugacityCoefficientL(double, double, double, double) - Method in class nce.phprop.eosgas.GasEos
-
Evaluate compressed liquid fugacity coefficient
- evalFugacityCoefficientL(double, double, double, double) - Method in class nce.phprop.eosgas.GasEosRK
-
- evalFugacityCoefficientL(double, double, double, double) - Method in class nce.phprop.eosgas.GasEosVDW
-
- evalFugacityCoefficientV(double, double, double) - Method in class nce.phprop.eosgas.GasEos
-
Evaluates pure species vapor phase fugacity coefficient
- evalFugacityCoefficientV(double, double, double) - Method in class nce.phprop.eosgas.GasEosRK
-
- evalFugacityCoefficientV(double, double, double) - Method in class nce.phprop.eosgas.GasEosVDW
-
- evalFugacityCoefficientV(double, double, double) - Method in class nce.phprop.eosgas.GasEosVirial
-
- evalFugacityL(double, double, double, double) - Method in class nce.phprop.eosgas.GasEos
-
- evalFugacityV(double, double, double) - Method in class nce.phprop.eosgas.GasEos
-
Evaluates pure species vapor phase fugacity
- evalFunction(double[]) - Method in class nce.datasets.models.DataFitModelAntoine
-
- evalFunction(double[]) - Method in class nce.datasets.models.DataFitModelSpecHeatEqnTrig
-
- evalFunction(double[]) - Method in class nce.datasets.models.DataFitModelSpecHeatPoly2
-
- evalFunction(double[]) - Method in class nce.datasets.models.DataFitModelWilson
-
- evalFunction(double) - Method in class nce.math.FuncR1R1
-
- evalFunction(double[], double[]) - Method in class nce.math.HomotopyFunc
-
- evalFunction(double) - Method in class nce.piping.PipePressDropAdiab
-
Objective function: y(outP) = 0
- evalFunction(double) - Method in class nce.piping.PipePressDropIsoth
-
objective function
- evalFunction(double) - Method in class nce.piping.PipePressDropOF
-
- evalGrashoff(double, double, double, double, double, double) - Static method in class nce.heattransfer.HT
-
Evaluates Grashoff number: Gr = l^3 * rho^2 * g * beta * dt / mu^2;
- evalHeatFluxBody1(double...) - Method in class nce.heattransfer.radiation.ConvexBody
-
- evalHeatFluxBody1(double...) - Method in class nce.heattransfer.radiation.EnclosedBody
-
- evalHeatFluxBody1(double...) - Method in class nce.heattransfer.radiation.EnclosedBodySmall
-
- evalHeatFluxBody1(double...) - Method in class nce.heattransfer.radiation.RadiationCase
-
Evaluates radiating heat flux emitted by body 1
- evalHeatFluxBody2(double...) - Method in class nce.heattransfer.radiation.ConvexBody
-
Not applicable for this radiation case.
- evalHeatFluxBody2(double...) - Method in class nce.heattransfer.radiation.EnclosedBody
-
- evalHeatFluxBody2(double...) - Method in class nce.heattransfer.radiation.EnclosedBodySmall
-
- evalHeatFluxBody2(double...) - Method in class nce.heattransfer.radiation.RadiationCase
-
Evaluates radiating heat flux emitted by body 2
- evalHeatPower12(double...) - Method in class nce.heattransfer.radiation.ConvexBody
-
Evaluates the radiant heat emitted from body 1 at temperature T.
- evalHeatPower12(double...) - Method in class nce.heattransfer.radiation.EnclosedBody
-
- evalHeatPower12(double...) - Method in class nce.heattransfer.radiation.EnclosedBodySmall
-
- evalHeatPower12(double...) - Method in class nce.heattransfer.radiation.RadiationCase
-
Evaluates the net radiating heat power transferred from body 1 to body 2
- evalHeatRelease(double, double) - Method in class nce.base.ChemicalSpecies
-
Evaluates heat release using the predefined equation.
- evalHeatRelease(double, double) - Method in class nce.heattransfer.HeatReleaseModel
-
Evaluates heat release by interpolation in a data set table
- evalHeatRelease(double, double) - Method in class nce.stream.Stream
-
- evalHeatReleaseAtAllSteps() - Method in class nce.equipments.HeatExchangerSide
-
Evaluates the heat release at all steps.
- evalHeatTransferArea() - Method in class nce.equipments.doublepipe.HeatExchangerDoublePipe
-
- evalHeatTransferArea() - Method in class nce.equipments.HeatExchanger
-
Evaluates heat transfer area on the base of the assigned geometry.
- evalHydDiameterForHeatTransfer(Object) - Method in class nce.equipments.doublepipe.HeatExchangerDoublePipeShellSide
-
- evalHydDiameterForHeatTransfer(Object) - Method in class nce.equipments.doublepipe.HeatExchangerDoublePipeTubeSide
-
- evalHydDiameterForHeatTransfer(Object) - Method in class nce.equipments.HeatExchangerSide
-
- evalHydDiameterForPressureDrop(Object) - Method in class nce.equipments.doublepipe.HeatExchangerDoublePipeShellSide
-
- evalHydDiameterForPressureDrop(Object) - Method in class nce.equipments.doublepipe.HeatExchangerDoublePipeTubeSide
-
- evalHydDiameterForPressureDrop(Object) - Method in class nce.equipments.HeatExchangerSide
-
- evalIrreversibleExpansion() - Method in class nce.equipments.Throttle
-
- evalJacobian(double[], double[]) - Method in class nce.math.FuncRnRn
-
Evaluation of Jacobian matrix by forward difference scheme Input: X,
- evalKinematicViscosity(double, double) - Method in class nce.phprop.viscosity.ViscosityEqnAstmD341
-
Evaluates kinematic viscosity with ASTM D341 equation
- evalKinematicViscosityCentiStokes(double, double) - Method in class nce.phprop.viscosity.ViscosityEqnAstmD341
-
Evaluates kinematic viscosity with ASTM D341 equation.
- evalLinearProfileWithFinalExtVal(String, double, double) - Method in class nce.base.DomainDecomposition
-
- evalLinearProfileWithStartExtVal(String, double, double) - Method in class nce.base.DomainDecomposition
-
- evalLiquidVolume(double, double) - Method in class nce.phprop.eosgas.GasEos
-
Evaluates liquid molar volume with eos.
- evalLiquidVolume(double, double) - Method in class nce.phprop.eosgas.GasEosIdeal
-
- evalLiquidVolume(double, double) - Method in class nce.phprop.eosgas.GasEosPR
-
- evalLiquidVolume(double, double) - Method in class nce.phprop.eosgas.GasEosRK
-
- evalLiquidVolume(double, double) - Method in class nce.phprop.eosgas.GasEosSRK
-
- evalLiquidVolume(double, double) - Method in class nce.phprop.eosgas.GasEosVDW
-
- evalLiquidVolume(double, double) - Method in class nce.phprop.eosgas.GasEosVirial
-
- evalLiquidVolumeWithEos(double, double) - Method in class nce.base.ChemicalSpecies
-
Evaluation of liquid molar volume with an equation of state
- evalLiquidVolumeWithEqn(double, double) - Method in class nce.base.ChemicalSpecies
-
Evaluates liquid molar volume with the predefined model equation.
- evalLockMartParameter(double, double, double, double, double) - Method in class nce.piping.PipePressDropLockhartMartinelli
-
Evaluates Lockhart - Martinelli parameter
- evalLockMartParameter(double, double, double, double, double) - Method in class nce.piping.PipeTwoPhaseDensity
-
Evaluates Lockhart - Martinelli parameter
- evalMach() - Method in class nce.piping.Pipe
-
Evaluates Mach number at inlet conditions
- evalMassVelocity() - Method in class nce.piping.Pipe
-
Evaluates mass velocity from available data
- evalMAWP() - Method in class nce.mech.CylinderASMEVIIId1UG27
-
Evaluates Maximum Allowable Working Pressure
- evalMAWP() - Method in class nce.mech.CylinderASMEVIIId1UG28
-
Evaluates MAWP
- evalMAWP() - Method in class nce.mech.ShellHeadASMEVIIId1UG32
-
Evaluates Maximum Allowable Working Pressure
- evalMAWP() - Method in class nce.mech.TruncatedConeASMEVIIId1UG32
-
Evaluates Maximum Allowable Working Pressure
- evalMinThickness() - Method in class nce.mech.BackingDeviceTEMA
-
Evaluates minimum required thickness
- evalMinThickness() - Method in class nce.mech.CylinderASMEVIIId1UG27
-
Evaluates required minimum thickness.
- evalMinThickness() - Method in class nce.mech.ShellHeadASMEVIIId1UG32
-
Evaluates required minimum thickness
- evalMinThickness() - Method in class nce.mech.TruncatedConeASMEVIIId1UG32
-
Evaluates required minimum thickness
- evalMinThickness() - Method in class nce.mech.Tubesheet
-
- evalNumericalDerivative(double) - Method in class nce.math.FuncR1R1
-
Computes the first derivative using the 3 point formula,
with an error O(h^2)
- evalNumericalDerivative5p(double) - Method in class nce.math.FuncR1R1
-
Computes the first derivative using the 5 point formula,
with an error O(h^4).
- evalNumericalDerivativeII(double) - Method in class nce.math.FuncR1R1
-
Computes the second derivative using the 3 point formula,
with an error O(h^2)
- evalNumericalDerivativeII5p(double) - Method in class nce.math.FuncR1R1
-
Computes the 2nd derivative using the 5 point formula, with an error O(h^4)
- evalNumericalDerivatives12(double) - Method in class nce.math.FuncR1R1
-
Computes the first and second derivative using the 3 point formula and
the same step h.
- evalNusselt(double...) - Method in class nce.heattransfer.forcedconvection.ForcedConvectionCorrelation
-
- evalNusselt(double...) - Method in class nce.heattransfer.forcedconvection.Generic
-
- evalNusselt(double...) - Method in class nce.heattransfer.forcedconvection.PetukovKirilov
-
- evalNusselt(double...) - Method in class nce.heattransfer.forcedconvection.PipeDittusBoelterCooling
-
- evalNusselt(double...) - Method in class nce.heattransfer.forcedconvection.PipeDittusBoelterHeating
-
- evalNusselt(double...) - Method in class nce.heattransfer.forcedconvection.PipeLaminarSiederTate
-
- evalNusselt(double...) - Method in class nce.heattransfer.forcedconvection.PipeSmooth
-
- evalNusselt(double...) - Method in class nce.heattransfer.forcedconvection.PipeTransition
-
- evalNusselt(double...) - Method in class nce.heattransfer.forcedconvection.PipeTurbulentSiederTate
-
- evalNusselt(double...) - Method in class nce.heattransfer.naturalconvection.ChiltonColburnGenerauxVernon
-
- evalNusselt(double...) - Method in class nce.heattransfer.naturalconvection.ChurchillChuCylinder
-
- evalNusselt(double...) - Method in class nce.heattransfer.naturalconvection.ChurchillChuFlatSurface
-
- evalNusselt(double...) - Method in class nce.heattransfer.naturalconvection.HorizontalCylinder
-
- evalNusselt(double...) - Method in class nce.heattransfer.naturalconvection.KatoNishiwakiHirata
-
- evalNusselt(double...) - Method in class nce.heattransfer.naturalconvection.KayansayanFinPipe
-
- evalNusselt(double...) - Method in class nce.heattransfer.naturalconvection.McAdamsDownward
-
- evalNusselt(double...) - Method in class nce.heattransfer.naturalconvection.McAdamsUpward
-
- evalNusselt(double...) - Method in class nce.heattransfer.naturalconvection.NaturalConvectionCorrelation
-
- evalNusselt(double...) - Method in class nce.heattransfer.naturalconvection.VerticalSurface
-
- evalOverdesign() - Method in class nce.mech.CylinderASMEVIIId1UG27
-
Evaluates thickness overdesign
- evalOverdesign() - Method in class nce.mech.CylinderASMEVIIId1UG28
-
Evaluates and overdesign using MAWP and design pressure
- evalOverdesign() - Method in class nce.mech.ShellHeadASMEVIIId1UG32
-
- evalOverdesign() - Method in class nce.mech.TruncatedConeASMEVIIId1UG32
-
- evalPrandtl(double, double, double) - Static method in class nce.heattransfer.HT
-
Evaluates Prandtl number: Pr = cp * mu / k
- evalPrandtl() - Method in class nce.stream.Stream
-
Evaluates stream Prandtl number using stored physical properties
- evalPrandtlAtAllSteps(DomainDecomposition) - Static method in class nce.heattransfer.HT
-
Evaluates Prandtl number at all grid steps
- evalPressure(double, double) - Method in class nce.phprop.eosgas.GasEos
-
Evalutes fluid pressure with eos.
- evalPressure(double, double) - Method in class nce.phprop.eosgas.GasEosIdeal
-
- evalPressure(double, double) - Method in class nce.phprop.eosgas.GasEosPR
-
- evalPressure(double, double) - Method in class nce.phprop.eosgas.GasEosRK
-
- evalPressure(double, double) - Method in class nce.phprop.eosgas.GasEosSRK
-
- evalPressure(double, double) - Method in class nce.phprop.eosgas.GasEosVDW
-
- evalPressure(double, double) - Method in class nce.phprop.eosgas.GasEosVirial
-
- evalPressureDrop() - Method in class nce.piping.Pipe
-
High level driver for pressure drop computation, uses preset flow regime
- evalPressureDrop(Pipe.FlowRegimeDeltaP) - Method in class nce.piping.Pipe
-
High level driver for pressure drop computation, sets also flow regime
- evalPressureWithEos(double, double) - Method in class nce.base.ChemicalSpecies
-
Evaluation of P(V, T) by an equation of state
- evalRadiationFactor12(double, double) - Method in class nce.heattransfer.radiation.RadiationCase
-
Radiation factor, maximum theoretical radiant heat that body 1 can
transfert to body 2
- evalRePrAtAllSteps() - Method in class nce.equipments.HeatExchangerSide
-
Evaluate Reynolds, Prandtl at all grid points setting also transport
properties.
- evalResidualEnthalpyL(double, double, double) - Method in class nce.phprop.eosgas.GasEos
-
- evalResidualEnthalpyL(double, double, double) - Method in class nce.phprop.eosgas.GasEosVDW
-
- evalResidualEnthalpyV(double, double, double) - Method in class nce.phprop.eosgas.GasEos
-
Evaluates vapor phase residual entropy from the definition
- evalResidualEnthalpyV(double, double, double) - Method in class nce.phprop.eosgas.GasEosRK
-
- evalResidualEnthalpyV(double, double, double) - Method in class nce.phprop.eosgas.GasEosVDW
-
- evalResidualEnthalpyV(double, double, double) - Method in class nce.phprop.eosgas.GasEosVirial
-
- evalResidualEntropyL(double, double, double) - Method in class nce.phprop.eosgas.GasEos
-
- evalResidualEntropyL(double, double, double) - Method in class nce.phprop.eosgas.GasEosVDW
-
- evalResidualEntropyV(double, double, double) - Method in class nce.phprop.eosgas.GasEos
-
Evaluates vapor phase residual entropy by numerical differentiation of
the equation of state at constant pressure.
- evalResidualEntropyV(double, double, double) - Method in class nce.phprop.eosgas.GasEosPR
-
- evalResidualEntropyV(double, double, double) - Method in class nce.phprop.eosgas.GasEosRK
-
- evalResidualEntropyV(double, double, double) - Method in class nce.phprop.eosgas.GasEosVDW
-
- evalResidualEntropyV(double, double, double) - Method in class nce.phprop.eosgas.GasEosVirial
-
- evalResidualGibbsFreeEnergyL(double, double, double) - Method in class nce.phprop.eosgas.GasEos
-
Not implemented.
- evalResidualGibbsFreeEnergyV(double, double, double) - Method in class nce.phprop.eosgas.GasEos
-
Evaluates vapor phase residual Gibbs free energy by numerical integration
of the equation of state at constant temperature.
- evalResidualInternalEnergyV(double, double, double) - Method in class nce.phprop.eosgas.GasEos
-
- evalReynolds(double, double, double, double) - Method in class nce.piping.Pipe
-
Evaluates Reynolds number and sets whether flow regime is laminar,
transition or turbulent
- evalReynoldsAtAllSteps(DomainDecomposition) - Static method in class nce.heattransfer.HT
-
Evaluates Reynolds number at all grid steps
- evalRootMeanSquareErr(double[], double[]) - Static method in class nce.math.NCEMath
-
Evaluates the root mean square error of dx = x1 - x2
- evalRootMeanSquareSum(double[]) - Static method in class nce.math.NCEMath
-
Evaluates the root mean square sum of f
- evalRugosityRel() - Method in class nce.piping.Pipe
-
Evaluates relative rugosity
- evalSatLiquidVolumeWithEqn(double) - Method in class nce.base.ChemicalSpecies
-
Evaluates liquid molar volume at saturation the predefined model equation.
- evalSatP(double) - Method in class nce.phprop.vaporpressure.VaporPressureAntoine
-
- evalSatP(double) - Method in class nce.phprop.vaporpressure.VaporPressureLeeKesler
-
- evalSatP(double) - Method in class nce.phprop.vaporpressure.VaporPressureModel
-
- evalSatPressure(double) - Method in class nce.base.ChemicalSpecies
-
Evaluates saturation pressure using the model specified in
'activeVaporPressureModel' variable
For example, to use an the equation call
useVaporPressureModel(ChemicalSpecies.VaporPressureModels.EQUATION)
- evalSatPressure(double, double) - Method in class nce.phprop.eosgas.GasEos
-
Evaluates fluid vapor pressure by Maxwell's rule
- evalSatPressure(double, double) - Method in class nce.phprop.eosgas.GasEosIdeal
-
- evalSatPressureWithEqn(double) - Method in class nce.base.ChemicalSpecies
-
- evalSatT(double) - Method in class nce.phprop.vaporpressure.VaporPressureAntoine
-
- evalSatT(double) - Method in class nce.phprop.vaporpressure.VaporPressureLeeKesler
-
- evalSatT(double) - Method in class nce.phprop.vaporpressure.VaporPressureModel
-
- evalSatTemperature(double) - Method in class nce.base.ChemicalSpecies
-
High level driver, evaluates saturation temperature using the model
specified in 'activeVaporPressureModel' variable
For example, to use an the equation call
useVaporPressureModel(ChemicalSpecies.VaporPressureModels.EQUATION)
- evalSatTemperatureWithEqn(double) - Method in class nce.base.ChemicalSpecies
-
- evalSlipRatio(double, double, double, double, double) - Method in class nce.piping.PipePressDropLockhartMartinelli
-
Evaluates two phase slip ratio, i.e.
- evalSlipRatio(double, double, double, double, double) - Method in class nce.piping.PipePressDropMSC
-
Evaluates two phase slip ratio using the method of Lockhart-Martinelli
with the two phase multiplier from the method of Muller-Steinhagen-Heck
- evalSlipRatio(double, double, double, double, double) - Method in class nce.piping.PipeTwoPhaseDensity
-
Evaluates two phase slip ratio, i.e.
- evalSpecHeat(double) - Method in class nce.databank.Material
-
- evalSpecificHeat(double) - Method in class nce.base.ChemicalSpecies
-
Evaluates Cp with the specific heat eqn as function of T
- evalSpecificHeat(double) - Method in class nce.stream.Stream
-
High level driver for specific heat computation.
- evalSpecificHeatIntH(double, double) - Method in class nce.base.ChemicalSpecies
-
Evaluates the integral Cp useful for enthalpy calculations:
Cp_av = Int_T0^T Cp dT; then H = Cp_av * (T - T0)
- evalSpecificHeatIntH(double, double) - Method in class nce.stream.Stream
-
High level driver for integral specific heat computation in enthalpy
calculations.
- evalSpecificHeatIntS(double, double) - Method in class nce.base.ChemicalSpecies
-
Evaluates the integral Cp useful for entropy calculations
(Cp/T)_av = Int_T0^T Cp dT
(Cp/T) = Int_T0^T (Cp / T) dT; then S = (Cp/T)_av * (T - T0)
- evalSpecificHeatIntS(double, double) - Method in class nce.stream.Stream
-
High level driver for integral specific heat computation in entropy
calculations.
- evalSpeedSoundIdealGas() - Method in class nce.stream.Stream
-
Evaluates speed of sound in a gas stream using the ideal gas equation
Following variables shall be set: cp/cv, temperature, mole mass
- evalSpeedSoundRealGas() - Method in class nce.stream.Stream
-
Evaluates the speed of sound (acoustic velocity) in a gas stream using the
real gas equation.
- evalSysK() - Method in class nce.vle.VleSolver
-
Evaluates Ki = yi / xi for every component i
- evalSysK() - Method in class nce.vle.VleSolverGamma
-
- evalSysK() - Method in class nce.vle.VleSolverRaoult
-
- evalTemperature(double, double) - Method in class nce.phprop.eosgas.GasEos
-
Evaluates fluid temperature with eos.
- evalTemperature(double, double) - Method in class nce.phprop.eosgas.GasEosIdeal
-
- evalTemperature(double, double) - Method in class nce.phprop.eosgas.GasEosPR
-
- evalTemperature(double, double) - Method in class nce.phprop.eosgas.GasEosRK
-
- evalTemperature(double, double) - Method in class nce.phprop.eosgas.GasEosSRK
-
- evalTemperature(double, double) - Method in class nce.phprop.eosgas.GasEosVDW
-
- evalTemperature(double, double) - Method in class nce.phprop.eosgas.GasEosVirial
-
- evalTemperatureWithEos(double, double) - Method in class nce.base.ChemicalSpecies
-
Evaluation of fluid absolute temperature with and equation of state
- evalThermalBalance() - Method in class nce.equipments.HeatExchanger
-
Closes thermal balance of the heat exchanger.
- evalThermalConductivity(double) - Method in class nce.databank.Material
-
- evalThermCond(double, double) - Method in class nce.base.ChemicalSpecies
-
Evaluates thermal conductivity with the predefined equation.
- evalThermCond(double, double) - Method in class nce.phprop.thermcond.ThermCondDataSet
-
Evaluates thermal conductivity by interpolation in a data set table
- evalThermCond(double, double) - Method in class nce.phprop.thermcond.ThermCondEqnFixed
-
- evalThermCond(double, double) - Method in class nce.phprop.thermcond.ThermCondEqnPoly3
-
- evalThermCond(double, double) - Method in class nce.phprop.thermcond.ThermCondEqnPoly5
-
- evalThermCond(double, double) - Method in class nce.phprop.thermcond.ThermCondGasPureHighP
-
- evalThermCond(double, double) - Method in class nce.phprop.thermcond.ThermCondHydrocGasPureLowP
-
- evalThermCond(double, double) - Method in class nce.phprop.thermcond.ThermCondHydrocLiq
-
- evalThermCond(double, double) - Method in class nce.phprop.thermcond.ThermCondMixRuleGasLowP
-
- evalThermCond(double, double) - Method in class nce.phprop.thermcond.ThermCondModel
-
- evalThermCond(double) - Method in class nce.phprop.thermcond.ThermCondModel
-
- evalThermCond(double, double) - Method in class nce.phprop.thermcond.ThermCondNonHydrocGasPureLowP
-
- evalThermCond(double, double) - Method in class nce.stream.Stream
-
High level driver, evaluates stream thermal conductivity [W/m degK]
- evalTwoPhaseMultiplier() - Method in class nce.piping.PipePressDropLockhartMartinelli
-
- evalTwoPhaseMultiplier() - Method in class nce.piping.PipePressDropMSC
-
- evalTwoPhaseMultiplier() - Method in class nce.piping.PipeTwoPhaseDensity
-
Pure implementation of the method Lokhart - Martinelli
This method invokes all sub-methods to evaluate also two phase density,
slip ratio and void fraction
- evalVaporDensityWithEos(double, double) - Method in class nce.stream.Stream
-
- evalVaporVolume(double, double) - Method in class nce.phprop.eosgas.GasEos
-
Evaluates vapor molar volume with eos.
- evalVaporVolume(double, double) - Method in class nce.phprop.eosgas.GasEosIdeal
-
- evalVaporVolume(double, double) - Method in class nce.phprop.eosgas.GasEosPR
-
- evalVaporVolume(double, double) - Method in class nce.phprop.eosgas.GasEosRK
-
- evalVaporVolume(double, double) - Method in class nce.phprop.eosgas.GasEosSRK
-
- evalVaporVolume(double, double) - Method in class nce.phprop.eosgas.GasEosVDW
-
- evalVaporVolume(double, double) - Method in class nce.phprop.eosgas.GasEosVirial
-
- evalVaporVolumeWithEos(double, double) - Method in class nce.base.ChemicalSpecies
-
Evaluation of Vv(P, T) by an equation of state
- evalVaporVolumeWithEos(double, double) - Method in class nce.stream.Stream
-
- evalViscosity(double, double) - Method in class nce.base.ChemicalSpecies
-
Evaluates species viscosity using the predefined equation.
- evalViscosity(double) - Method in class nce.databank.Material
-
- evalViscosity(double, double) - Method in class nce.phprop.viscosity.HydrocarbonPureVapor
-
- evalViscosity(double, double) - Method in class nce.phprop.viscosity.ViscosityDataSet
-
Evaluates viscosity by interpolation in a data set table
- evalViscosity(double, double) - Method in class nce.phprop.viscosity.ViscosityEqnAstmD341
-
- evalViscosity(double, double) - Method in class nce.phprop.viscosity.ViscosityEqnFixed
-
- evalViscosity(double, double) - Method in class nce.phprop.viscosity.ViscosityEqnGasPowLawPowSeries
-
- evalViscosity(double, double) - Method in class nce.phprop.viscosity.ViscosityEqnGasReichenberg
-
- evalViscosity(double, double) - Method in class nce.phprop.viscosity.ViscosityEqnGasSutherland
-
- evalViscosity(double, double) - Method in class nce.phprop.viscosity.ViscosityEqnLiqRiedelModif
-
- evalViscosity(double, double) - Method in class nce.phprop.viscosity.ViscosityEqnLiqVelzen
-
- evalViscosity(double, double) - Method in class nce.phprop.viscosity.ViscosityEqnPoly3
-
- evalViscosity(double, double) - Method in class nce.phprop.viscosity.ViscosityEqnPoly5
-
- evalViscosity(double, double) - Method in class nce.phprop.viscosity.ViscosityGasDeanStielPressCorrec
-
- evalViscosity(double, double) - Method in class nce.phprop.viscosity.ViscosityMixRuleGasBromleyWilke
-
Applies mixing rule evaluating also species viscosity
- evalViscosity(double, double) - Method in class nce.phprop.viscosity.ViscosityMixRuleLiq
-
Applies mixing rule evaluating also species viscosity
ln(mu) = sum_i(x_i * ln(mu_i)) mu = exp(ln(mu))
- evalViscosity(double, double) - Method in class nce.phprop.viscosity.ViscosityModel
-
- evalViscosity(double) - Method in class nce.phprop.viscosity.ViscosityModel
-
- evalViscosity(double, double) - Method in class nce.stream.Stream
-
High level driver, evaluates stream viscosity [Pa s]
- evalVolFlowAtAllSteps(DomainDecomposition) - Static method in class nce.heattransfer.HT
-
Evaluates volumetric flow at all grid steps
- evalVolume(double, double) - Method in class nce.phprop.molvolume.LiqMolVolFixed
-
- evalVolume(double, double) - Method in class nce.phprop.molvolume.LiqMolVolHBT
-
- evalVolume(double, double) - Method in class nce.phprop.molvolume.LiqMolVolModel
-
- evalVolume(double, double) - Method in class nce.phprop.molvolume.LiqMolVolRackett
-
- evalVolume(double, double) - Method in class nce.phprop.molvolume.LiqMolVolRSD
-
- evalVolumeExpansivity(double) - Method in class nce.databank.Material
-
- evalVolumeExpansivity(double, double) - Method in class nce.phprop.density.DensityModel
-
Evaluate volume expansion coefficient beta from fluid density
- evalVolumeSat(double) - Method in class nce.phprop.molvolume.LiqMolVolFixed
-
- evalVolumeSat(double) - Method in class nce.phprop.molvolume.LiqMolVolHBT
-
- evalVolumeSat(double) - Method in class nce.phprop.molvolume.LiqMolVolModel
-
- evalVolumeSat(double) - Method in class nce.phprop.molvolume.LiqMolVolRackett
-
- evalVolumeSat(double) - Method in class nce.phprop.molvolume.LiqMolVolRSD
-
- evalZ() - Method in class nce.phprop.eosgas.GasEos
-
An alias for evalZv
- evalZl(double, double) - Method in class nce.phprop.eosgas.GasEos
-
- evalZl() - Method in class nce.phprop.eosgas.GasEos
-
Calculates liquid phase compressibility factor Z with previously setted
state variables P, Vl,T
- evalZl(double, double) - Method in class nce.phprop.eosgas.GasEosRK
-
- evalZl(double, double) - Method in class nce.phprop.eosgas.GasEosVDW
-
- evalZv(double, double) - Method in class nce.phprop.eosgas.GasEos
-
- evalZv() - Method in class nce.phprop.eosgas.GasEos
-
Calculates vapor phase compressibility factor Z with previously
setted state variables P, Vv, T
- evalZv(double, double) - Method in class nce.phprop.eosgas.GasEosRK
-
- evalZv(double, double) - Method in class nce.phprop.eosgas.GasEosVDW
-
- evalZv(double, double) - Method in class nce.phprop.eosgas.GasEosVirial
-
- ExcGibbsEn - Class in nce.vle
-
Basic class for Excess Gibbs Energy models
- ExcGibbsEn() - Constructor for class nce.vle.ExcGibbsEn
-
- ExcGibbsEnWilson - Class in nce.vle
-
Wilson model for excess Gibbs free energy
- ExcGibbsEnWilson(int) - Constructor for class nce.vle.ExcGibbsEnWilson
-
- extractActiveParameters(double[]) - Method in class nce.datasets.DataFitModel
-