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):021302-021302-13. doi:10.1115/1.4040929 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)

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):021302-021302-13. doi:10.1115/1.4040929 Figure Legend: Percentage of the terminated and nonterminated particles during simulation time

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):021302-021302-13. doi:10.1115/1.4040929 Figure Legend: Percentage of nonterminated particles of different sizes for the simulation times after 3.5 s

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):021302-021302-13. doi:10.1115/1.4040929 Figure Legend: Cumulative length distribution of collected particles within simulation times

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):021302-021302-13. doi:10.1115/1.4040929 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)

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):021302-021302-13. doi:10.1115/1.4040929 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 0.025 m)

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):021302-021302-13. doi:10.1115/1.4040929 Figure Legend: The hexahedral surface mesh and tetrahedral inlets mesh for Hortlax gasifier geometry

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):021302-021302-13. doi:10.1115/1.4040929 Figure Legend: Cumulative and normal volume-based distribution of particles in different diameters

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):021302-021302-13. doi:10.1115/1.4040929 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

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):021302-021302-13. doi:10.1115/1.4040929 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)

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):021302-021302-13. doi:10.1115/1.4040929 Figure Legend: Typical behaviors of the predicted particle trajectories for different diameters

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):021302-021302-13. doi:10.1115/1.4040929 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).

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):021302-021302-13. doi:10.1115/1.4040929 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