When a liquid particle impinges a wall, the particle may deform and remain in direct contact with the wall for a short period of time before rebounding. During this time, heat is exchanged between the particle and the wall.
For droplet-to-wall heat transfer calculations, the Ansys Fluent discrete phase model assumes that the droplet deforms to a cylinder when impacting the wall (see Figure 12.16: Geometric Parameters of Deformed Impinging Droplet in Heat Transfer Calculations).
Then the heat transfer from the wall to the droplet is given as:
(12–349) |
where | |
= droplet particle mass (kg) | |
= droplet specific heat (J/kg/K) | |
= particle temperature (K) | |
= effective particle-wall contact area (m2) | |
= particle center-point to wall distance (m) | |
= droplet thermal conductivity (W/m/K) | |
= wall temperature (K) |
The effective particle-wall contact area is calculated by time-averaging the particle-wall contact area assuming a sinusoidal particle diameter variation from 0 to the maximum spreading diameter during contact period [65]. The maximum spreading diameter is computed according to [11] as:
(12–350) |
(12–351) |
where | |
= droplet diameter before impact (m) | |
= Impact Weber number |
The contact time is calculated as [65]:
(12–352) |
where | |
= constant with the default value of 0.4 | |
= particle density (kg/m3 ) | |
= surface tension (N/m) |
The heat exchange between the wall and the particle is calculated by integrating Equation 12–349 over the contact time . The increase of the droplet temperature is limited by the boiling point.
For each wall face, the particle-to-wall energy transfer is computed by summing the energy contributions from all particle parcels hitting the wall face and is then added to the heat flux of the wall.