Heat Transfer

Heat transfer causes physical particles (droplets, bubble, solid particles) to heat or to cool according to the temperature of their environment. When the phases are one-way coupled, the continuous phase does not change temperature, even when the particles do. In two-way coupled cases, the heat transfer contributes to both the continuous phase and the dispersed phase, but with different signs so the net heat transfer flux is zero.

For a single particle, the heat transfer is defined as:

Figure 1. EQUATION_DISPLAY
Q=hcoefA(Tp-T)
(2854)

where hcoef is the heat transfer coefficient, A is the area of the particle, and Tp and T are the particle and background temperatures, respectively.

In a continuous approach such as dispersed multiphase (in contrast to a discrete approach such as Lagrangian multiphase), the heat transfer can be expressed as:

Figure 2. EQUATION_DISPLAY
Q¯cd=h¯coef,d(6αdD)(Td-T)
(2855)

where:

  • Q¯cd is the averaged heat flux between the dispersed and the continuous phase. It is defined as positive for heat flowing from the particles to the background.
  • h¯coef,d the averaged heat transfer coefficient of the dispersed phase
  • Td,T are the temperatures of the dispersed and the continuous phase, respectively
Ranz-Marshall
The heat transfer coefficient is computed in terms of the Nusselt number:
Figure 3. EQUATION_DISPLAY
hcoef=kNupD
(2856)

where k is the thermal conductivity, D is the diameter of the dispersed phase, and Nup is the particle Nusselt number.

The Nusselt number correlates as:

Figure 4. EQUATION_DISPLAY
Nu p = 2 ( 1 + 0.3 Re p 1 / 2 Pr 1 / 3 )
(2857)

where Re p is the particle Reynolds number and Pr is the Prandlt number.