1. From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
Date of download: 11/6/2018
Copyright © ASME. All rights reserved.
From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
J. Fluids Eng. 2018;141(2): doi: /
Figure Legend:
Cyclone configuration scheme studied by Obermair et al. [6]; left: side view, right: top view (D is cyclone body diameter = 0.4 m; vortex finder wall thickness is 0.01 m)

2. From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
Date of download: 11/6/2018
Copyright © ASME. All rights reserved.
From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
J. Fluids Eng. 2018;141(2): doi: /
Figure Legend:
Percentage of the terminated and nonterminated particles during simulation time

3. From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
Date of download: 11/6/2018
Copyright © ASME. All rights reserved.
From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
J. Fluids Eng. 2018;141(2): doi: /
Figure Legend:
Percentage of nonterminated particles of different sizes for the simulation times after 3.5 s

4. From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
Date of download: 11/6/2018
Copyright © ASME. All rights reserved.
From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
J. Fluids Eng. 2018;141(2): doi: /
Figure Legend:
Cumulative length distribution of collected particles within simulation times

5. From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
Date of download: 11/6/2018
Copyright © ASME. All rights reserved.
From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
J. Fluids Eng. 2018;141(2): doi: /
Figure Legend:
Tangential gas velocity profiles for four various axial positions in the drop tube: (a) z/D=−0.1, (b) z/D=−0.575, (c) z/D=−0.695, and (d) z/D=−1.02 (n is number rate)

6. From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
Date of download: 11/6/2018
Copyright © ASME. All rights reserved.
From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
J. Fluids Eng. 2018;141(2): doi: /
Figure Legend:
Cyclone geometry and coordinate system of the Hortlax gasifier plant; left: side view, right: tope view (D is gasifier body diameter = 0.750 m; vortex finder wall thickness is m)

7. From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
Date of download: 11/6/2018
Copyright © ASME. All rights reserved.
From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
J. Fluids Eng. 2018;141(2): doi: /
Figure Legend:
The hexahedral surface mesh and tetrahedral inlets mesh for Hortlax gasifier geometry

8. From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
Date of download: 11/6/2018
Copyright © ASME. All rights reserved.
From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
J. Fluids Eng. 2018;141(2): doi: /
Figure Legend:
Cumulative and normal volume-based distribution of particles in different diameters

9. From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
Date of download: 11/6/2018
Copyright © ASME. All rights reserved.
From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
J. Fluids Eng. 2018;141(2): doi: /
Figure Legend:
Dimensionless radial profile of the time-averaged tangential and axial velocities at four different axial positions on the YZ plane (X = 0) from the single-phase simulation of the Hortlax cyclone

10. From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
Date of download: 11/6/2018
Copyright © ASME. All rights reserved.
From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
J. Fluids Eng. 2018;141(2): doi: /
Figure Legend:
The contour plots for the times-averaged: (a) static pressure, (b) tangential velocity, (c) axial velocity, and (d) radial velocity at YZ plane (X = 0)

11. From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
Date of download: 11/6/2018
Copyright © ASME. All rights reserved.
From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
J. Fluids Eng. 2018;141(2): doi: /
Figure Legend:
Typical behaviors of the predicted particle trajectories for different diameters

12. From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
Date of download: 11/6/2018
Copyright © ASME. All rights reserved.
From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
J. Fluids Eng. 2018;141(2): doi: /
Figure Legend:
Radial profiles of the time-averaged gas flow for single-phase and two-way coupled gas–solid flows (from left to right: tangential velocity, axial velocity. From top to bottom: the horizontal levels are z/D = 2.93, 2.13, 1.33, 0.67).

13. From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
Date of download: 11/6/2018
Copyright © ASME. All rights reserved.
From: Modeling of Particle-Laden Cold Flow in a Cyclone Gasifier
J. Fluids Eng. 2018;141(2): doi: /
Figure Legend:
The difference between the monitored time-averaged pressure over the cross-sectional area in the inlet tube and the cross-sectional area close to the outlet in the vortex finder tube from the two-way coupled gas–solid simulation