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Public Member Functions | |
TypeName ("liquid") | |
declareRunTimeSelectionTable (autoPtr, liquid,,(),()) | |
declareRunTimeSelectionTable (autoPtr, liquid, Istream,(Istream &is),(is)) | |
liquid (scalar W, scalar Tc, scalar Pc, scalar Vc, scalar Zc, scalar Tt, scalar Pt, scalar Tb, scalar dipm, scalar omega, scalar delta) | |
Construct from components. | |
liquid (Istream &is) | |
Construct from Istream. | |
virtual | ~liquid () |
scalar | W () const |
Molecular weight [kg/kmol]. | |
scalar | Tc () const |
Critical temperature [K]. | |
scalar | Pc () const |
Critical pressure [Pa]. | |
scalar | Vc () const |
Critical volume [m^3/mol]. | |
scalar | Zc () const |
Critical compressibilty factor. | |
scalar | Tt () const |
Triple point temperature [K]. | |
scalar | Pt () const |
Triple point pressure [Pa]. | |
scalar | Tb () const |
Normal boiling temperature [K]. | |
scalar | dipm () const |
Dipole moment []. | |
scalar | omega () const |
Pitzer's ascentric factor []. | |
scalar | delta () const |
Solubility parameter [(J/m^3)^(1/2)]. | |
virtual scalar | rho (scalar p, scalar T) const =0 |
Liquid rho [kg/m^3]. | |
virtual scalar | pv (scalar p, scalar T) const =0 |
Vapour pressure [Pa]. | |
virtual scalar | hl (scalar p, scalar T) const =0 |
Heat of vapourisation [J/kg]. | |
virtual scalar | cp (scalar p, scalar T) const =0 |
Liquid heat capacity [J/(kg K)]. | |
virtual scalar | h (scalar p, scalar T) const =0 |
Liquid h [J/kg]. | |
virtual scalar | cpg (scalar p, scalar T) const =0 |
Ideal gas heat capacity [J/(kg K)]. | |
virtual scalar | mu (scalar p, scalar T) const =0 |
Liquid viscosity [Pa s]. | |
virtual scalar | mug (scalar p, scalar T) const =0 |
Vapour viscosity [Pa s]. | |
virtual scalar | K (scalar p, scalar T) const =0 |
Liquid thermal conductivity [W/(m K)]. | |
virtual scalar | Kg (scalar p, scalar T) const =0 |
Vapour thermal conductivity [W/(m K)]. | |
virtual scalar | sigma (scalar p, scalar T) const =0 |
Surface tension [N/m]. | |
virtual scalar | D (scalar p, scalar T) const =0 |
Vapour diffussivity [m2/s]. | |
virtual void | writeData (Ostream &os) const |
Write the function coefficients. | |
Static Public Member Functions | |
autoPtr< liquid > | New (Istream &is) |
Return a pointer to a new liquid created from input. | |
Friends | |
Ostream & | operator<< (Ostream &os, const liquid &l) |
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Construct from components.
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Construct from Istream.
Definition at line 160 of file liquid.H. References readScalar. |
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Liquid heat capacity [J/(kg K)].
Implemented in aC10H7CH3, Ar, bC10H7CH3, C10H22, C12H26, C13H28, C14H30, C16H34, C2H5OH, C2H6, C2H6O, C3H6O, C3H8, C4H10O, C6H14, C6H6, C7H16, C7H8, C8H10, C8H18, C9H20, CH3OH, H2O, IC8H18, IDEA, MB, and N2. |
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Ideal gas heat capacity [J/(kg K)].
Implemented in aC10H7CH3, Ar, bC10H7CH3, C10H22, C12H26, C13H28, C14H30, C16H34, C2H5OH, C2H6, C2H6O, C3H6O, C3H8, C4H10O, C6H14, C6H6, C7H16, C7H8, C8H10, C8H18, C9H20, CH3OH, H2O, IC8H18, IDEA, MB, and N2. |
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Vapour diffussivity [m2/s].
Implemented in aC10H7CH3, Ar, bC10H7CH3, C10H22, C12H26, C13H28, C14H30, C16H34, C2H5OH, C2H6, C2H6O, C3H6O, C3H8, C4H10O, C6H14, C6H6, C7H16, C7H8, C8H10, C8H18, C9H20, CH3OH, H2O, IC8H18, IDEA, MB, and N2. |
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Solubility parameter [(J/m^3)^(1/2)].
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Dipole moment [].
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Liquid h [J/kg].
Implemented in aC10H7CH3, Ar, bC10H7CH3, C10H22, C12H26, C13H28, C14H30, C16H34, C2H5OH, C2H6, C2H6O, C3H6O, C3H8, C4H10O, C6H14, C6H6, C7H16, C7H8, C8H10, C8H18, C9H20, CH3OH, H2O, IC8H18, IDEA, MB, and N2. |
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Heat of vapourisation [J/kg].
Implemented in aC10H7CH3, Ar, bC10H7CH3, C10H22, C12H26, C13H28, C14H30, C16H34, C2H5OH, C2H6, C2H6O, C3H6O, C3H8, C4H10O, C6H14, C6H6, C7H16, C7H8, C8H10, C8H18, C9H20, CH3OH, H2O, IC8H18, IDEA, MB, and N2. |
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Liquid thermal conductivity [W/(m K)].
Implemented in aC10H7CH3, Ar, bC10H7CH3, C10H22, C12H26, C13H28, C14H30, C16H34, C2H5OH, C2H6, C2H6O, C3H6O, C3H8, C4H10O, C6H14, C6H6, C7H16, C7H8, C8H10, C8H18, C9H20, CH3OH, H2O, IC8H18, IDEA, MB, and N2. |
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Vapour thermal conductivity [W/(m K)].
Implemented in aC10H7CH3, Ar, bC10H7CH3, C10H22, C12H26, C13H28, C14H30, C16H34, C2H5OH, C2H6, C2H6O, C3H6O, C3H8, C4H10O, C6H14, C6H6, C7H16, C7H8, C8H10, C8H18, C9H20, CH3OH, H2O, IC8H18, IDEA, MB, and N2. |
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Liquid viscosity [Pa s].
Implemented in aC10H7CH3, Ar, bC10H7CH3, C10H22, C12H26, C13H28, C14H30, C16H34, C2H5OH, C2H6, C2H6O, C3H6O, C3H8, C4H10O, C6H14, C6H6, C7H16, C7H8, C8H10, C8H18, C9H20, CH3OH, H2O, IC8H18, IDEA, MB, and N2. |
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Vapour viscosity [Pa s].
Implemented in aC10H7CH3, Ar, bC10H7CH3, C10H22, C12H26, C13H28, C14H30, C16H34, C2H5OH, C2H6, C2H6O, C3H6O, C3H8, C4H10O, C6H14, C6H6, C7H16, C7H8, C8H10, C8H18, C9H20, CH3OH, H2O, IC8H18, IDEA, MB, and N2. |
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Return a pointer to a new liquid created from input.
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Pitzer's ascentric factor [].
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Critical pressure [Pa].
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Triple point pressure [Pa].
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Vapour pressure [Pa].
Implemented in aC10H7CH3, Ar, bC10H7CH3, C10H22, C12H26, C13H28, C14H30, C16H34, C2H5OH, C2H6, C2H6O, C3H6O, C3H8, C4H10O, C6H14, C6H6, C7H16, C7H8, C8H10, C8H18, C9H20, CH3OH, H2O, IC8H18, IDEA, MB, and N2. |
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Liquid rho [kg/m^3].
Implemented in aC10H7CH3, Ar, bC10H7CH3, C10H22, C12H26, C13H28, C14H30, C16H34, C2H5OH, C2H6, C2H6O, C3H6O, C3H8, C4H10O, C6H14, C6H6, C7H16, C7H8, C8H10, C8H18, C9H20, CH3OH, H2O, IC8H18, IDEA, MB, and N2. |
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Surface tension [N/m].
Implemented in aC10H7CH3, Ar, bC10H7CH3, C10H22, C12H26, C13H28, C14H30, C16H34, C2H5OH, C2H6, C2H6O, C3H6O, C3H8, C4H10O, C6H14, C6H6, C7H16, C7H8, C8H10, C8H18, C9H20, CH3OH, H2O, IC8H18, IDEA, MB, and N2. |
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Normal boiling temperature [K].
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Critical temperature [K].
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Triple point temperature [K].
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Critical volume [m^3/mol].
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Molecular weight [kg/kmol].
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Write the function coefficients.
Reimplemented in aC10H7CH3, Ar, bC10H7CH3, C10H22, C12H26, C13H28, C14H30, C16H34, C2H5OH, C2H6, C2H6O, C3H6O, C3H8, C4H10O, C6H14, C6H6, C7H16, C7H8, C8H10, C8H18, C9H20, CH3OH, H2O, IC8H18, IDEA, MB, and N2. |
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Critical compressibilty factor.
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