Modifier and Type | Class and Description |
---|---|
class |
SpecHeatEqnDataSet
Specific heat is entered as a table of data
interpolation is made using the methods available in the
DataSet class
|
Modifier and Type | Class and Description |
---|---|
class |
ForcedConvectionCorrelation
Abstract factory class to be extended for the creation of forced convection
correlations.
|
class |
Generic
Evaluates Nusselt number as Nu = a * Re^e1 * Pr^e2 * (mu / mu_w)^e3
|
class |
PetukovKirilov
Petukov - Kirilov (1958) equation for Nusselt in a pipe
|
class |
PipeDittusBoelterCooling
Dittus-Boelter equation for Nusselt in a pipe, cooling
|
class |
PipeDittusBoelterHeating
Dittus-Boelter equation for Nusselt in a pipe, heating
|
class |
PipeLaminarSiederTate
Evaluates Nusselt number for laminar flow in a tube (smooth pipe) using
Sieder - Tate correlation.
|
class |
PipeSmooth
Evaluates Nusselt number in a tube (smooth pipe) choosing the correct
equation depending on flow type (laminar, transition, turbulent)
|
class |
PipeTransition
Evaluates Nusselt number for transition flow ia a tube (smooth pipe)
as a linear combination between laminar and turbulent flow computed
with Sieder - Tate equation
|
class |
PipeTurbulentSiederTate
Evaluates Nusselt number for turbulent flow in a tube (smooth pipe)
Maximum deviations +15% -10%.
|
Modifier and Type | Class and Description |
---|---|
class |
ChiltonColburnGenerauxVernon
Chilton - Colburn - Generaux - Vernon
Ref.
|
class |
ChurchillChuCylinder
Churchill - Chu 1975b for the estimation of Nusselt number for natural
convection over an isothermal horizontal cylinder
|
class |
ChurchillChuFlatSurface
Churchill - Chu for the estimation of Nusselt number for natural convection
over an isothermal vertical flat surface.
|
class |
HorizontalCylinder
Generic equation for natural convection over horizontal cylinder valid
for any Rayleight number and d < 8 in.
|
class |
KatoNishiwakiHirata
Kato - Nishiwaki - Hirata equation for natural convection over
vertical plates and cylinders
|
class |
KayansayanFinPipe
Natural convection over horizontal heater based on fin-and-tube heater with
circular fins, valid for any Rayleight number > 1e+7
Ref.: N.
|
class |
McAdamsDownward
McAdams equation for the estimation of Nusselt number for natural
convection over an isothermal horizontal heated flat surface with
facing downward
|
class |
McAdamsUpward
McAdams equation for the estimation of Nusselt number for natural
convection over an isothermal horizontal heated flat surface facing upward
|
class |
NaturalConvectionCorrelation
Base class to be extended to implement new natural convection models
|
class |
VerticalSurface
Generic equation for natural convection over vertical surfaces valid for
any Rayleight number
|
Modifier and Type | Class and Description |
---|---|
class |
ConvexBody
Radiant heat emitted from a convex gray body.
|
class |
EnclosedBody
Radiant heat transferred from body 1 enclosed into body 2, general case.
|
class |
EnclosedBodySmall
Radiant heat transferred from body 1 enclosed into body 2, were
Area2 >> Area1, eg.
|
class |
RadiationCase
Generic class for heat radiation computations
|
Modifier and Type | Class and Description |
---|---|
class |
DensityDataSet
Density is modeled via a data set.
|
class |
DensityEqnFixed |
class |
DensityEqnPow
Power law model for density
|
class |
DensityMixRuleIdealLiquid
Mixing rule for the density of liquids
|
class |
DensityModel
This class of models is for mass/volume density
|
Modifier and Type | Class and Description |
---|---|
class |
GasEos
Equation of state object.
|
class |
GasEosIdeal
Ideal gas equation of state
|
class |
GasEosPR
Peng - Robinson cubic equation of state
|
class |
GasEosRK
Redlich - Kwong cubic equation of state
|
class |
GasEosSRK
Soave cubic equation of state
|
class |
GasEosVDW
Van der Waals cubic equation of state.
|
class |
GasEosVirial
Virial equation of state, truncated at 2nd term.
|
Modifier and Type | Class and Description |
---|---|
class |
LiqMolVolFixed
Trivial model for liquid molar volume: constant
|
class |
LiqMolVolHBT
Hankinson-Brobst-Thomson technique for estimation of saturated liquid
molar volume.
|
class |
LiqMolVolModel
Base class for the definition of liquids molar volume equations
|
class |
LiqMolVolRackett
Rackett equation for molar volume of SATURATED liquids.
|
class |
LiqMolVolRSD
Rackett - Spencer - Danner equation for molar volume of SATURATED liquids.
|
Modifier and Type | Class and Description |
---|---|
class |
SpecHeatDataSet
TODO
|
class |
SpecHeatEqnFixed
Heat capacity constant with temperature
|
class |
SpecHeatEqnPoly2
Modified 2nd order polynomial expression (Ref.
|
class |
SpecHeatEqnPoly5
TODO to be compleated
|
class |
SpecHeatEqnTrig
Mixed formula with powers and hyperbolic functions (Ref.
|
class |
SpecHeatMixRuleIdeal
Evaluates the mole averaged specific heat of gaseous or liquid ideal mixture
|
class |
SpecHeatMixRuleIdealMass
Evaluates the mass averaged specific heat of an ideal mixture
|
class |
SpecHeatModel
Base class for the definition of a specific heat equation
|
Modifier and Type | Class and Description |
---|---|
class |
ThermCondDataSet |
class |
ThermCondEqnFixed |
class |
ThermCondEqnPoly3 |
class |
ThermCondEqnPoly5 |
class |
ThermCondGasPureHighP
Estimation of thermal conductivity of pure gases above atmospheric pressure,
with the method of Stiel and Thodos.
|
class |
ThermCondHydrocGasPureLowP
Method recommended by Misic and Thodos for the thermal conductivity of
pure hydrocarbon gases at P < 350 kPa.
|
class |
ThermCondHydrocLiq
Thermal conductivity of pure component hydrocarbon liquids
|
class |
ThermCondMixRuleGasLowP
Wassiljeva's mixing rule for the thermal conductivity of low pressure gases
|
class |
ThermCondModel |
class |
ThermCondNonHydrocGasPureLowP
Method recommended for the thermal conductivity of pure non-hydrocarbon gases
at P <= 1 bar
|
Modifier and Type | Class and Description |
---|---|
class |
VaporPressureAntoine
Classic Antoine equation
|
class |
VaporPressureLeeKesler
The Lee - Kesler corresponding states method for vapor pressure
|
class |
VaporPressureModel
Base class for the definition of a vapour pressure equation
|
Modifier and Type | Class and Description |
---|---|
class |
HydrocarbonPureVapor
Estimates the viscosity of pure hydrocarbons at low pressure
at Tr < 0.6 with the method of Stiel and Thodos.
|
class |
ViscosityDataSet |
class |
ViscosityEqnAstmD341
ASTM D341 equation for kinematic viscosity
|
class |
ViscosityEqnFixed
Constant value model for viscosity
|
class |
ViscosityEqnGasPowLawPowSeries
Equation for VAPOR viscosity correlation by a modified power law and
power series expansion
Ref.
|
class |
ViscosityEqnGasReichenberg
Estimates the viscosity of pure nonhydrocarbon polar gases at low pressure by
the method of Reichenberg
|
class |
ViscosityEqnGasSutherland
Method to estimate gas viscosity at temperature T known the value at
temperature T0.
|
class |
ViscosityEqnLiqRiedelModif
Equation for LIQUID viscosity correlation by a modified Riedel equation
Ref.
|
class |
ViscosityEqnLiqVelzen
Method for by Velzen for the estimation of the viscosity of
pure hydrocarbon and pure
nonhydrocarbon liquids based on group contributions.
|
class |
ViscosityEqnPoly3 |
class |
ViscosityEqnPoly5 |
class |
ViscosityGasDeanStielPressCorrec
Estimates the viscosity of gaseous hydrocarbons and mixtures of hydrocarbons
at high pressure above Pr of 0.6 by the method of Dean and Stiel.
|
class |
ViscosityMixRuleGasBromleyWilke
Mixing rule applicable to gaseous mixture of hydrocarbons and non
hydrocarbons suggested by Bromley and Wilke
Ref.
|
class |
ViscosityMixRuleLiq
Mixing rule for non-hydrocarbon liquid mixtures viscosity.
|
class |
ViscosityModel |