The influences of loading ratios and conveying velocity on gas-solid two phase flow characteristics: a comprehensive experimental CFD-DEM study
- 27 May 2020
- journal article
- research article
- Published by Taylor & Francis in International Journal of Ambient Energy
- Vol. 43 (1) , 2714-2726
Abstract
At this present research paper, solid particles jet into turbulent cross flow trajectories and turbulence structure adaptations are presented for a non-reacting (No combustion) flow conditions. Additionally, the particle-source-in cell (PSI-CELL) methodology is used to achieve coupled (CFD-DEM) calculations. In following research paper, a fully real fine sized jet of Polyethylene with a mean diameter of (3.6 mm) has been taken as the solid jet into the carrier phase. The conveying velocity and the solid particles loading ratios during the experiments were varied from 7 m/s to 12 m/s, and 0.270, 0.610, 0.950, respectively. Both experimental and simulated findings reveal that the gas-phase velocity pattern in the horizontal direction takes an asymmetrical trend with solid increased particles loading ratio below the lower portion of the cylindrical channel. The findings of simulation and experiments demonstrate that the turbulence intensity within both radial and central areas of the cylindrical channel is greater than those presented in near-wall areas. Evidently, the velocity and pressure of the main flow field will decrease. There are improvements in the turbulence intensity about (240%) in some areas along with cross-section of the cylindrical channel.Keywords
This publication has 30 references indexed in Scilit:
- Experimental study of particle-driven secondary flow in turbulent pipe flowsJournal of Fluid Mechanics, 2012
- Dilute-phase pneumatic conveying of polystyrene particles: pressure drop curve and particle distribution over the pipe cross-sectionBrazilian Journal of Chemical Engineering, 2011
- Turbulence modulation in dilute particle-laden flowInternational Journal of Heat and Fluid Flow, 2009
- Hydrodynamic modelling of dense gas-fluidised beds: comparison and validation of 3D discrete particle and continuum modelsPowder Technology, 2004
- Numerical Models for Two-Phase Turbulent FlowsAnnual Review of Fluid Mechanics, 1996
- Drag coefficient and terminal velocity of spherical and nonspherical particlesPowder Technology, 1989
- Effect of particle size on modulating turbulent intensityInternational Journal of Multiphase Flow, 1989
- A short note on the drag correlation for spheresPowder Technology, 1986
- Equation of motion for a small rigid sphere in a nonuniform flowThe Physics of Fluids, 1983
- LDV measurements of an air–-solid two-phase flow in a horizontal pipeJournal of Fluid Mechanics, 1982