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humidityTemperatureCoupledMixedFvPatchScalarField Class Reference

Mixed boundary condition for temperature to be used at the coupling interface between fluid solid regions. More...

#include <humidityTemperatureCoupledMixedFvPatchScalarField.H>

Detailed Description

Mixed boundary condition for temperature to be used at the coupling interface between fluid solid regions.

This boundary condition can operate in four modes:

  • constantMass: thermal inertia only
    • requires rho, thickness and cp
  • condensation: condensation only
    • when the wall temperature (Tw) is below the dew temperature (Tdew) condesation takes place and the resulting condensed mass is stored on the wall
  • evaporation: evaporation only
    • initial mass is vaporized when Tw is above the input vaporization temperature (Tvap).
  • condensationAndEvaporation : condensation and evaporation take place simultaneously.

There is no mass flow on the wall, i.e. the mass condensed on a face remains on that face. It uses a 'lumped mass' model to include thermal inertia effects.

It assumes a drop-wise type of condensation, whereby its heat transfer Nusselt number is calculated using:

\begin{eqnarray*}    51104 + 2044 (T - 273.15)   & T > 295 & T < 373 \\
    255510                      & T > 373 &
\end{eqnarray*}

References:

    Standard models (tag:BLID):
        Bergman, T. L., Lavine, A. S.,
        Incropera, F. P., & Dewitt, D. P. (2011).
        Fundamentals of heat and mass transfer.
        John Wiley & Sons. 7th Edition. Chapter 10.
        ISBN:9780470501979

The mass transfer correlation used is:

\‍[ h_m = D_{ab} \frac{Sh}{L} \‍]

where:

$        D_{ab} $=mass vapour difussivity
$        L      $=characteristic length
$        Sh     $=Sherwood number

The Sherwood number is calculated using:

\begin{eqnarray*}            0.664 Re^\frac{1}{2} Sc^\frac{1}{3} & Re < 5.0E+05 \\
            0.037 Re^\frac{4}{5} Sc^\frac{1}{3} & Re > 5.0E+05
\end{eqnarray*}

where:

$        Re     $=Reynolds number
$        Sc     $=Schmidt number

NOTE:

  • The correlation used to calculate Tdew is for water vapour.
  • A scalar transport equation for the carrier specie is required, e.g. supplied via a function object or in the main solver. This specie transports the vapour phase in the main ragion.
  • The boundary condition of this specie on the coupled wall must be fixedGradient in order to allow condensation or evaporation of the vapour in or out of this wall
  • Addition of extra layers in possible using thicknessLayers and kappaLayers

Example usage:

On the fluid side

    myInterfacePatchName
    {
        type            thermalHumidityCoupledMixed;
        kappaMethod     fluidThermo;
        kappa           none;

        // Modes of operation: inert, condensation, vaporization, condEvap
        mode            condEvap;

        // Carrier species name
        specieName      H2O;

        // Carrier molecular weight
        carrierMolWeight           28.9;

        // Characteristic length of the wall
        L               0.1;

        // Vaporisation temperature
        Tvap            273;

        // Liquid properties for the condensed mass
        liquid
        {
            H2O
            {
                defaultCoeffs       yes;
            }
        }

        thicknessLayers (0.1 0.2 0.3 0.4);
        kappaLayers     (1 2 3 4);

        // thickness, density and cp required for inert and condensation
        // modes

        //thickness       uniform 0;
        //cp              uniform 0;
        //rho             uniform 0;

        value           $internalField;
    }

On the solid side:

    myInterfacePatchName
    {
        type            thermalInertiaMassTransferCoupledMixed;
        kappaMethod     solidThermo;
        kappa           none;
        value           uniform 260;
    }
Source files

The documentation for this class was generated from the following file: