In this problem, the energy equation and the species conservation equations will be solved, along with the momentum and continuity equations.
1.
Enable heat transfer by enabling the energy equation.
ModelsEnergyEdit...
(a)
Enable
Energy Equation.
(b)
Click
OK to close the
Energy dialog box.
2.
Enable chemical species transport
and reaction.
ModelsSpeciesEdit...
Although you enable reactions, you still run a non-reacting flow to produce an initial solution. You will run reacting flow in step 8.
(a)
Select
Species Transport in the
Model list.
The
Species Model dialog box will expand to show relevant input options.
(b)
Enable
Volumetric and
Wall Surface in the
Reactions group box.
(c)
Enable
Mass Deposition Source in the
Wall Surface Reaction Options group box.
Mass Deposition Source is enabled because there is a certain loss of mass due to the surface deposition
reaction, i.e., As(s) and Ga(s) are being deposited out. If you were to do an overall mass balance without taking this fact into account, you would end up with a slight imbalance.
(d)
Enable
Inlet Diffusion in the
Options group box.
(e)
Retain the default setting for
Diffusion Energy Source.
This includes the effect of enthalpy
transport due to species diffusion
in the energy equation, which contributes to the energy balance, especially for the case of Lewis numbers
far from unity.
(f)
Enable
Full Multicomponent Diffusion and
Thermal Diffusion.
The
Full Multicomponent Diffusion activates Stefan-Maxwell's equations and computes the diffusive fluxes of all species in the mixture to all concentration gradients. The
Thermal Diffusion effects cause heavy molecules to diffuse less rapidly, and light molecules to diffuse more rapidly, toward heated surfaces.
(g)
Click
OK to close the
Species Model dialog box.
ANSYS FLUENT will list the properties in the console, that are required for the models that you have enabled.
An
Information dialog box will open reminding you to confirm the property values that have been extracted from the database.