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Journal Articles
Accepted Manuscript
Journal:
Journal of Fluids Engineering
Article Type: Research-Article
J. Fluids Eng.
Paper No: FE-22-1561
Published Online: February 4, 2023
Journal Articles
Accepted Manuscript
Journal:
Journal of Fluids Engineering
Article Type: Research-Article
J. Fluids Eng.
Paper No: FE-22-1477
Published Online: February 4, 2023
Journal Articles
Journal:
Journal of Fluids Engineering
Article Type: Research-Article
J. Fluids Eng. April 2023, 145(4): 041204.
Paper No: FE-22-1110
Published Online: February 1, 2023
Journal Articles
Journal:
Journal of Fluids Engineering
Article Type: Research-Article
J. Fluids Eng. May 2023, 145(5): 051401.
Paper No: FE-22-1369
Published Online: February 1, 2023
Journal Articles
Journal:
Journal of Fluids Engineering
Article Type: Research-Article
J. Fluids Eng. April 2023, 145(4): 041403.
Paper No: FE-22-1245
Published Online: February 1, 2023
Journal Articles
Journal:
Journal of Fluids Engineering
Article Type: Research-Article
J. Fluids Eng. May 2023, 145(5): 051201.
Paper No: FE-22-1443
Published Online: February 1, 2023
Image
in Predicting Behavior of Gas-Solids Systems for Non-Uniform Fluidization
> Journal of Fluids Engineering
Published Online: February 1, 2023
Fig. 1 Example of divisions within a multicomponent bed More
Image
in Predicting Behavior of Gas-Solids Systems for Non-Uniform Fluidization
> Journal of Fluids Engineering
Published Online: February 1, 2023
Fig. 2 Typical curve for pressure drop versus inlet gas velocity for ( a ) single-component system and ( b ) multicomponent system More
Image
in Predicting Behavior of Gas-Solids Systems for Non-Uniform Fluidization
> Journal of Fluids Engineering
Published Online: February 1, 2023
Fig. 3 Representation of pressure drop versus inlet gas velocity to demonstrate the discretization scheme for the mixture and components More
Image
in Predicting Behavior of Gas-Solids Systems for Non-Uniform Fluidization
> Journal of Fluids Engineering
Published Online: February 1, 2023
Fig. 4 Single-component mixture pressure drop versus inlet gas velocity comparing experiments, MFiX and MASS method for a glass bead fluidized bed [ 10 ] More
Image
in Predicting Behavior of Gas-Solids Systems for Non-Uniform Fluidization
> Journal of Fluids Engineering
Published Online: February 1, 2023
Fig. 5 Binary mixture pressure drop versus inlet gas velocity comparing experiments, MFiX and MASS method for glass beads with ( a ) case 2 composed of 499 μ m and 172 μ m diameter particles and ( b ) case 3 composed of 499 μ m and 271 μ m diameter particles [ 49 ] More
Image
in Predicting Behavior of Gas-Solids Systems for Non-Uniform Fluidization
> Journal of Fluids Engineering
Published Online: February 1, 2023
Fig. 6 Ternary mixture pressure drop versus inlet gas velocity comparing experiments, MFiX and MASS method for dolomite diameters of 517, 392, and 322 μ m and respective initial mass fractions for ( a ) 35%, 35%, and 30%; ( b )40%, 40%, and 20%; and ( c ) 45%, 45%, and 10% [ 6 ] More
Image
in Predicting Behavior of Gas-Solids Systems for Non-Uniform Fluidization
> Journal of Fluids Engineering
Published Online: February 1, 2023
Fig. 7 Ternary mixture pressure drop versus inlet gas velocity comparing experiments, MFiX and MASS method for ( a ) cases 7, ( b ) case 8, and ( c ) case 9 More
Image
in Predicting Behavior of Gas-Solids Systems for Non-Uniform Fluidization
> Journal of Fluids Engineering
Published Online: February 1, 2023
Fig. 8 Predicted U mf,predict versus experimental U mf,expt for cases 1, 3, and 4 for ( a ) all data, ( b ) case 3, and ( c ) cases 1 and 4. Dashed lines (– – –) ±10%, (– · –) ±25%, and (– · · –) ±50% relative error. More
Image
in Behavior of Gas–Solid Two-Phase Flow in a Backward Facing Step - Effect of Interparticle Collisions
> Journal of Fluids Engineering
Published Online: February 1, 2023
Fig. 1 ( a ) Schematic of the computational domain and ( b ) axial variation of the static pressure along the channel More
Image
in Behavior of Gas–Solid Two-Phase Flow in a Backward Facing Step - Effect of Interparticle Collisions
> Journal of Fluids Engineering
Published Online: February 1, 2023
Fig. 2 Comparison of the computed velocity profiles of the solid phase with the experimental data of Ruck and Makiola [ 27 ] at different axial locations in the downstream channel More
Image
in Behavior of Gas–Solid Two-Phase Flow in a Backward Facing Step - Effect of Interparticle Collisions
> Journal of Fluids Engineering
Published Online: February 1, 2023
Fig. 3 Comparison of the computed r.m.s. velocity profiles of the gas-phase with the experimental data of Ruck and Makiola [ 27 ] at different axial locations in the downstream. More
Image
in Behavior of Gas–Solid Two-Phase Flow in a Backward Facing Step - Effect of Interparticle Collisions
> Journal of Fluids Engineering
Published Online: February 1, 2023
Fig. 4 Mesh independent More
Image
in Behavior of Gas–Solid Two-Phase Flow in a Backward Facing Step - Effect of Interparticle Collisions
> Journal of Fluids Engineering
Published Online: February 1, 2023
Fig. 5 Effect of interparticle restitution coefficient on the loss coefficient under different ( a ) particle sizes ( b ) solid-phase volume solid fractions, and ( c ) solid particle densities More
Image
in Behavior of Gas–Solid Two-Phase Flow in a Backward Facing Step - Effect of Interparticle Collisions
> Journal of Fluids Engineering
Published Online: February 1, 2023
Fig. 6 Effect of interparticle restitution coefficient on the circulation strength of the gas-phase More