Javascript is required
Search

Acadlore takes over the publication of IJCMEM from 2025 Vol. 13, No. 3. The preceding volumes were published under a CC BY 4.0 license by the previous owner, and displayed here as agreed between Acadlore and the previous owner. ✯ : This issue/volume is not published by Acadlore.

Open Access
Research article

CFD and Experimental Approach on Three Phase Gas-Liquid-Solid Newtonian Fluid Flow in Horizontal Pipes

Rasel A Sultan1,
Serag Alfarek1,
M. A. Rahman2,
Sohrab Zendehboudi1
1
Faculty of Engineering and Applied Science, Memorial University of Newfoundland, Canada.
2
Petroleum Engineering Program, Texas A&M University, Qatar.
International Journal of Computational Methods and Experimental Measurements
|
Volume 7, Issue 1, 2019
|
Pages 33-44
Received: N/A,
Revised: N/A,
Accepted: N/A,
Available online: N/A
View Full Article|Download PDF

Abstract:

This study analyses three dimensional fluid flow through horizontal pipelines with three-phase gas- liquid-solid Newtonian fluids by Computational Fluid Dynamics (CFD) simulation. Validating the simulation with experimental data, the study aims to develop a versatile acceptable simulation model that can be used further for different applied cases. An experimental setup is developed in our laboratory to determine slug flow (air-water) through a horizontal pipeline. Air as gas, water as liquid and silica as solid particle is used in this work. ANSYS Fluent version 16.2 is employed to perform the simulation. The Eulerian multiphase model with the Reynolds Stress Model (RSM) turbulence closure is adopted to analyse multiphase fluid flow. Parameters are selected from experimental works to validate the simula- tion. After a good agreement with experimental data, sensitivity analysis is conducted to observe the three phase fluid flow characteristics through horizontal flow. Pressure gradient (pressure drop per unit length) and in situ concentration profile are used as primary parameters. This article provides a clear relationship between the different parameters of three-phase fluid flow through a horizontal pipeline.

Keywords: CFD, experimental setup, pipeline, pressure gradient, slug flow, slurry flow, three phase flow.


Cite this:
APA Style
IEEE Style
BibTex Style
MLA Style
Chicago Style
GB-T-7714-2015
Sultan, R. A., Alfarek, S., Rahman, M. A., & Zendehboudi, S. (2019). CFD and Experimental Approach on Three Phase Gas-Liquid-Solid Newtonian Fluid Flow in Horizontal Pipes. Int. J. Comput. Methods Exp. Meas., 7(1), 33-44. https://doi.org/10.2495/CMEM-V7-N1-33-44
R. A. Sultan, S. Alfarek, M. A. Rahman, and S. Zendehboudi, "CFD and Experimental Approach on Three Phase Gas-Liquid-Solid Newtonian Fluid Flow in Horizontal Pipes," Int. J. Comput. Methods Exp. Meas., vol. 7, no. 1, pp. 33-44, 2019. https://doi.org/10.2495/CMEM-V7-N1-33-44
@research-article{Sultan2019CFDAE,
title={CFD and Experimental Approach on Three Phase Gas-Liquid-Solid Newtonian Fluid Flow in Horizontal Pipes},
author={Rasel A Sultan and Serag Alfarek and M. A. Rahman and Sohrab Zendehboudi},
journal={International Journal of Computational Methods and Experimental Measurements},
year={2019},
page={33-44},
doi={https://doi.org/10.2495/CMEM-V7-N1-33-44}
}
Rasel A Sultan, et al. "CFD and Experimental Approach on Three Phase Gas-Liquid-Solid Newtonian Fluid Flow in Horizontal Pipes." International Journal of Computational Methods and Experimental Measurements, v 7, pp 33-44. doi: https://doi.org/10.2495/CMEM-V7-N1-33-44
Rasel A Sultan, Serag Alfarek, M. A. Rahman and Sohrab Zendehboudi. "CFD and Experimental Approach on Three Phase Gas-Liquid-Solid Newtonian Fluid Flow in Horizontal Pipes." International Journal of Computational Methods and Experimental Measurements, 7, (2019): 33-44. doi: https://doi.org/10.2495/CMEM-V7-N1-33-44
SULTAN R A, ALFAREK S, RAHMAN M A, et al. CFD and Experimental Approach on Three Phase Gas-Liquid-Solid Newtonian Fluid Flow in Horizontal Pipes[J]. International Journal of Computational Methods and Experimental Measurements, 2019, 7(1): 33-44. https://doi.org/10.2495/CMEM-V7-N1-33-44