94 return sigma_.
f(p, T);
106 return D_.
f(p, T, Wb);
scalar f(scalar, scalar T) const
Evaluate the function and return the result.
scalar rho(scalar p, scalar T) const
Liquid density [kg/m^3].
scalar B(scalar p, scalar T) const
Second Virial Coefficient [m^3/kg].
scalar Cpg(scalar p, scalar T) const
Ideal gas heat capacity [J/(kg K)].
scalar h(scalar p, scalar T) const
Liquid Enthalpy [J/(kg)].
scalar f(scalar, scalar T) const
Evaluate the function and return the result.
scalar Kg(scalar p, scalar T) const
Vapour thermal conductivity [W/(m K)].
scalar D(scalar p, scalar T) const
Vapour diffussivity [m2/s].
scalar f(scalar, scalar T) const
Evaluate the function and return the result.
scalar f(scalar, scalar T) const
Evaluate the function and return the result.
scalar hl(scalar p, scalar T) const
Heat of vapourisation [J/kg].
scalar f(scalar, scalar T) const
Evaluate the function and return the result.
scalar sigma(scalar p, scalar T) const
Surface tension [N/m].
void T(FieldField< Field, Type > &f1, const FieldField< Field, Type > &f2)
scalar f(scalar, scalar T) const
Evaluate the function and return the result.
scalar pv(scalar p, scalar T) const
Vapour pressure [Pa].
scalar f(scalar p, scalar T) const
API vapour mass diffusivity function using properties from.
scalar mu(scalar p, scalar T) const
Liquid viscosity [Pa s].
scalar K(scalar p, scalar T) const
Liquid thermal conductivity [W/(m K)].
scalar mug(scalar p, scalar T) const
Vapour viscosity [Pa s].
scalar Cp(scalar p, scalar T) const
Liquid heat capacity [J/(kg K)].