What Methods Are Available for Exchanging Heat Transfer Coefficients?

For turbulent flows, the central concept for modeling convective heat transfer at the wall is given by the standard wall function, which can be written as:

Figure 1. EQUATION_DISPLAY
q˙w"=ρf(yc)Cp,f(yc)u*(y+(yc))T+(y+(yc))(TwTr)
(550)

where yc is the distance to the near wall cell center, y+ is the non-dimensional wall distance, u* is the reference velocity, and T+ is the non-dimensional temperature -- both of which are determined by the chosen wall treatment. ρf and Cp,f are the density and specific heat of the fluid. Note that ρf, Cp,f, u*, and T+ are functions of the distance from the wall.

Comparing Eqn. (550) with Eqn. (548), the heat transfer coefficient can be written as:

Figure 2. EQUATION_DISPLAY
h(yc)=ρf(yc)Cp,f(yc)u*(y+(yc))T+(y+(yc))
(551)

This expression is the foundation for various definitions of heat transfer coefficient in Simcenter STAR-CCM+. These coefficients, and their corresponding fluid reference temperatures, are listed in the table below.

Field Function Reference Temperature for Data Exchange
Local Heat Transfer Coefficient Local Heat Transfer Reference Temperature
Specified Y+ Heat Transfer Coefficient Specified Y+ Heat Transfer Reference Temperature
Heat Transfer Coefficient User-defined reference temperature
Virtual Local Heat Transfer Coefficient N/A

Local Heat Transfer Coefficient

This is the heat transfer coefficient evaluated at the centroid of the cell next to the boundary, that is h(y=yc). It is given by:

Figure 3. EQUATION_DISPLAY
hlocal=ρf(yc)Cp,f(yc)u*T+(y+(yc))
(552)

The corresponding fluid reference temperature is given by:

Figure 4. EQUATION_DISPLAY
Tlocal=Tw+q˙w"h
(553)

Specified Y+ Heat Transfer Coefficient

This is the heat transfer coefficient evaluated at a user specified value of y+, such that y+(y)=Yuser+. It follows that:

Figure 5. EQUATION_DISPLAY
hy+=ρf(yc)Cp,f(yc)u*T+(Yuser+)
(554)

The corresponding fluid reference temperature, the Specified Y+ Heat Transfer Reference Temperature is given by:

Figure 6. EQUATION_DISPLAY
Tf,y+=Tw+q˙w"hy+
(555)

As this definition does not guarantee that Tf,y+ lies within the temperature range of the local region, the following conditions are enforced to give realistic values:

Figure 7. EQUATION_DISPLAY
Tf,y+={Tw+q˙w"hy+TminTw+q˙w"hy+TmaxTminTw+q˙w"hy+<TminTmaxTw+q˙w"hy+>Tmax
(556)

In the latter two cases, hy+ will be re-evaluated such that

Figure 8. EQUATION_DISPLAY
hy+=q˙w"(Tf,y+Tw)
(557)
For these field functions, the y + value is set on the Specified Y+ Heat Transfer Coefficient field function node within Automation > Field Functions.

Virtual Local Heat Transfer Coefficient

This is an approximation to the true Local Heat Transfer Coefficient that does not require an energy model to be activated. It is defined as the heat transfer coefficient evaluated at y=yc, where yc is the distance of the near wall cell center from the wall.

Figure 9. EQUATION_DISPLAY
hvirtual=ρf(yc)Cp,f(yc)u*T+(y+(yc))
(558)
Since thermal material properties are not available, the specific heat, Cp,f is specified as a reference value, as well as the molecular and turbulent Prandtl numbers. These are set on the Virtual Local Heat Transfer Coefficient field function node, as shown below. The fluid density, ρf is obtained locally from the simulation.

Heat Transfer Coefficient

This is yet another choice for defining heat transfer coefficients. It is evaluated based on a specified bulk temperature Tbulk.

Figure 10. EQUATION_DISPLAY
hbulk=q˙w"(TbulkTw)
(559)

This definition does not guarantee that the evaluated heat transfer coefficient is positive. When exchanging data with other CAE codes, if the evaluated hbulk is not positive, then the local heat transfer coefficient, hlocal, and its corresponding reference temperature, Tlocal, are exchanged instead.

The bulk temperature is set as a property of the Heat Transfer Coefficient field function node.