Figures & data
Figure 1. Simulation schematic of the impinging jet with micron and submicron droplets: (a) 3D sketch; (b) scale and boundary conditions; (c) mesh setup.
![Figure 1. Simulation schematic of the impinging jet with micron and submicron droplets: (a) 3D sketch; (b) scale and boundary conditions; (c) mesh setup.](/cms/asset/69a14b25-5456-4c13-bed6-4705d6e383d0/uast_a_1740162_f0001_c.jpg)
Figure 2. Size distribution of the injected micro and nano droplets. The average diameter (Sauter mean diameter) of the droplets is 4.85 µm.
![Figure 2. Size distribution of the injected micro and nano droplets. The average diameter (Sauter mean diameter) of the droplets is 4.85 µm.](/cms/asset/00d34a0a-156a-4361-9b7f-113e3dfa46c6/uast_a_1740162_f0002_b.jpg)
Figure 3. Normalized velocity profiles and turbulence intensity in simulation compared with the experiment: (a) normalized velocity profile at z/D = 1 and z/D = 3; (b) normalized turbulence intensity at z/D = 1 and z/D = 3. z is the distance to the nozzle in streamwise direction and x is the distance to the centerline in radial direction.
![Figure 3. Normalized velocity profiles and turbulence intensity in simulation compared with the experiment: (a) normalized velocity profile at z/D = 1 and z/D = 3; (b) normalized turbulence intensity at z/D = 1 and z/D = 3. z is the distance to the nozzle in streamwise direction and x is the distance to the centerline in radial direction.](/cms/asset/09cd2b84-c78d-4baa-984a-abeae49cdb9a/uast_a_1740162_f0003_c.jpg)
Figure 4. Dual-ring deposition patterns in experiment and simulation: (a) experimental result where the gray level stands for the normalized thickness of the deposited liquid; (b) simulation result in two-way coupling method with coalescence being considered. The number for the different sized circles is the droplet diameter value in micron.
![Figure 4. Dual-ring deposition patterns in experiment and simulation: (a) experimental result where the gray level stands for the normalized thickness of the deposited liquid; (b) simulation result in two-way coupling method with coalescence being considered. The number for the different sized circles is the droplet diameter value in micron.](/cms/asset/d5e3d478-28e6-4c2b-870e-269b9a00bc01/uast_a_1740162_f0004_c.jpg)
Figure 5. Simulation results: (a) velocity profile in part of the computational region; (b) velocity vector in part of the computational region; (c) normalized turbulent intensity in a straight line near the plate, the distance between the line and the plate is 0.5 mm; (d) turbulence intensity distribution. The turbulence intensity near the wall is lower than the turbulence intensity away from the wall in the region near the outer ring.
![Figure 5. Simulation results: (a) velocity profile in part of the computational region; (b) velocity vector in part of the computational region; (c) normalized turbulent intensity in a straight line near the plate, the distance between the line and the plate is 0.5 mm; (d) turbulence intensity distribution. The turbulence intensity near the wall is lower than the turbulence intensity away from the wall in the region near the outer ring.](/cms/asset/f53beb25-4746-4a2f-958d-40a145842834/uast_a_1740162_f0005_c.jpg)
Figure 6. Relative thickness distributions under different droplets volume fractions: (a) αV = αV0.1; (b) αV = αV1 = 10−5; (c) αV = αV2; (d) αV = αV4; (e) αV = αV8. The modeling choice of the one or two-way coupling with or without coalescence calculation are compared.
![Figure 6. Relative thickness distributions under different droplets volume fractions: (a) αV = αV0.1; (b) αV = αV1 = 10−5; (c) αV = αV2; (d) αV = αV4; (e) αV = αV8. The modeling choice of the one or two-way coupling with or without coalescence calculation are compared.](/cms/asset/45f6c164-6e29-48f6-a8dd-eaa217adf43d/uast_a_1740162_f0006_c.jpg)