Transport Properties
After constructing a model, transport properties can be calculated (if respective parameters are available). The call for all this is always of the form:
transport_property(model, p, T, x=[1.]; phase=:unkwown)
where
model
is aAbstractTransportPropertyModel
,p
is the pressure ([p] = Pa
),T
is the temperature ([T] = K
),x
is the mole fraction ([x] = mol mol⁻¹
), andphase
is the desired phase (liquid
orgas
) used in the volume solver.
Internally, the density is always calculated first and then the function EntropyScaling.ϱT_transport_property(model, ϱ, T, x)
is called (with [ϱ] = mol m⁻³
).
EntropyScaling.viscosity
— Functionviscosity(model::EntropyScalingModel, p, T, z=[1.]; phase=:unknown)
Viscosity η(p,T,x)
([η] = Pa s
).
EntropyScaling.thermal_conductivity
— Functionthermal_conductivity(model::EntropyScalingModel, p, T, z=[1.]; phase=:unknown)
Thermal conductivity λ(p,T,x)
([λ] = W m⁻¹ K⁻¹
).
EntropyScaling.self_diffusion_coefficient
— Functionself_diffusion_coefficient(model::EntropyScalingModel, p, T, z=[1.]; phase=:unknown)
Self-diffusion coefficient D(p,T,x)
([D] = m² s⁻¹
).
EntropyScaling.MS_diffusion_coefficient
— FunctionMS_diffusion_coefficient(model::EntropyScalingModel, p, T, z; phase=:unknown)
Maxwell-Stefan diffusion coefficient Ð(p,T,x)
([Ð] = m² s⁻¹
).