To achieve the purpose of this study, it is essential to validate the use of CFD. The experimental results and cyclone dimensions were cited [
19,
20]. The geometric schematic diagram and dimension were represented as
Figure 5 and
Table 3, respectively. The mesh-independence test not only helps the efficient use of computing cost, but also obtains a numerically optimized computational domain [
21]. To verify the validity of the CFD, a mesh-independence test was performed by calculating the particle separation efficiency. The particle separation efficiency refers to the ratio of the total number of particles injected at the inlet and the number of particles collected in the dust container. The discreet phase modeling (DPM) was used to calculate the separation efficiency [
17]. The total number of particles are 10
4. The particle density is 2770 kg/m
3. The particle size distribution is divided to 10 class based on the Rosin–Rammler theory as Equation (6).
where the
is the mean diameter, and the
is the diffusion parameter. For simulation, the d and n are defined to 5 μm and 3.5 μm, respectively. Moreover, the distribution of particle diameters is set from 1 to 10 μm. The simulation results by decreasing mesh size were compared with the cited experimental data [
19]. The three mesh types as coarse, fine, and finest were used for mesh-independent test. The total number and mesh size of coarse types are
and 100 mm, respectively. The total number and mesh size of fine types are
and 6.5 mm, respectively. The total number and mesh size of coarse types are
and 3.5 mm, respectively. The near-wall treatment was achieved by using scalable wall functions considering the grid refinement with y
+ < 11. The growth from the wall is at a ratio of 1.5. The CFD results by three grid types were compared with the experimental data as
Table 4. As the mesh size decreases, the numerical values converged. The error between the CFD results and the referenced experimental results was within 2%. The grid size of fine type mesh was 6.5 mm. The fine type mesh was selected due to the numeric accuracy and computational cost in this study. Furthermore, the mesh quality check for the fine type mesh was performed as shown the
Table 5. The quality checking results show that the averaged skewness is 0.177 which represents the reasonable accuracy of mesh shape and the averaged aspect ratio of the fine mesh is about 1.814. Therefore, the fine type mesh is acceptable. The selected grid size is used as an input condition of CFD analysis for neural network modeling.
In addition, in order to select an appropriate turbulence model that can simulate a cyclone strong rotational flow, the results of the velocity distribution experiment [
20] and the prediction results according to the turbulence model were compared. The experimental data and simulation data were compared with the results of the tangential velocity and axial velocity distribution at the certain locations (Y = 0.77D,
) as shown
Figure 6. The residual values of the turbulence equation and mass equation showed the under
and
. In the
Figure 6, the x label is the distance from the center of the cyclone to the wall. When the
model was used, it showed an abnormal tangential distribution near the wall. The reason for this prediction is that the
model assumes anisotropic property for modeling the Reynolds stress term. When
model is applied for cyclone flow analysis, the outer flow and inner flow can be captured incorrectly. In contrast, Reynolds stress model (RSM) predicted a velocity distribution similar to the experimental results. The RSM can properly simulate rotational flow through an isotropic assumption for Reynolds stress term. Therefore, in this study, the RSM was applied to capture the cyclone flow. The detailed equations and explanations on the RSM can refer the reference [
17,
18].