Reynolds number dependence of gas-phase turbulence in particle-laden flows: Effects of particle inertia and particle loading

被引:18
作者
Hadinoto, Kunn [1 ]
Curtis, Jennifer Sinclair [2 ]
机构
[1] Nanyang Technol Univ, Sch Chem & Biomed Engn, Singapore 637459, Singapore
[2] Univ Florida, Dept Chem Engn, Gainesville, FL 32611 USA
关键词
Pneumatic conveying; Gas-particle flow; Turbulence modulation; Fluidization; NUMERICAL-SIMULATION; KINETIC-THEORY; VERTICAL PIPE; FLUID INERTIA; MODULATION;
D O I
10.1016/j.powtec.2009.05.022
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A gas-particle flow experiment at a low particle loading (m = 0.4) in a vertical downward pipe is conducted at three different Reynolds numbers (Re = 6000, 10.000, and 13,000) to investigate the Re influence on the gas-phase turbulence modulation. The mean and fluctuating velocity data of both phases are acquired using a two-component LDV/PDA system. Two particles of varying degrees of inertia (i.e. high-density 70 mu m glass beads and low-density 60 mu m cenospheres) are used as the model particles to examine the effect of particle inertia on the trend in the turbulence modulation as a function of Re. An experiment at a higher particle loading (m = 4,0) using the glass beads is also conducted to examine the effect of particle concentration. In the presence of high inertia particles (St(T)>500) at a low particle loading, the gas-phase turbulence intensity in the pipe core is increased with increasing Re resulting in turbulence enhancement relative to the unladen flow. The turbulence enhancement is attributed to 1) a modification of the turbulence production by the Reynolds stress due to interparticle collision and/or 2) a reduction in the fluctuating drag force due to a change in the radial profile of the particle concentration. In contrast, the gas-phase turbulence intensity in the presence of low inertia particles (St(T)<500) is found to decrease with increasing Re similar to the trend in the unladen flow. Lastly. the turbulence enhancement at high Re is not observed at a high particle loading where the turbulent energy dissipation by the fluctuating drag force is dominant. (c) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:119 / 127
页数:9
相关论文
共 25 条
[1]   The role of meso-scale structures in rapid gas-solid flows [J].
Agrawal, K ;
Loezos, PN ;
Syamlal, M ;
Sundaresan, S .
JOURNAL OF FLUID MECHANICS, 2001, 445 :151-185
[2]  
[Anonymous], 2001, FLUENT 6 0 USERS GUI
[3]   The influence of particle rotation on wake stability at particle Reynolds numbers, ReP&lt;300 -: implications for turbulence modulation in two-phase flows [J].
Best, JL .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1998, 24 (05) :693-720
[4]   Effect of collisions on the dispersed phase fluctuation in a dilute tube flow:: Experimental and theoretical analysis [J].
Caraman, N ;
Borée, J ;
Simonin, O .
PHYSICS OF FLUIDS, 2003, 15 (12) :3602-3612
[5]   ON PREDICTING PARTICLE-LADEN TURBULENT FLOWS [J].
ELGHOBASHI, S .
APPLIED SCIENTIFIC RESEARCH, 1994, 52 (04) :309-329
[6]   EFFECT OF PARTICLE-SIZE ON MODULATING TURBULENT INTENSITY [J].
GORE, RA ;
CROWE, CT .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 1989, 15 (02) :279-285
[7]   Reynolds number dependence of gas-phase turbulence in gas-particle flows [J].
Hadinoto, K ;
Jones, EN ;
Yurteri, C ;
Curtis, JS .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2005, 31 (04) :416-434
[8]   Effect of interstitial fluid on particle-particle interactions in kinetic theory approach of dilute turbulent fluid-particle flow [J].
Hadinoto, K ;
Curtis, JS .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (14) :3604-3615
[9]   Numerical simulation of the Reynolds number effect on gas-phase turbulence modulation [J].
Hadinoto, Kunn ;
Curtis, Jennifer Sinclair .
INTERNATIONAL JOURNAL OF MULTIPHASE FLOW, 2009, 35 (02) :129-141
[10]   VELOCITY AND PARTICLE-FLUX CHARACTERISTICS OF TURBULENT PARTICLE-LADEN JETS [J].
HARDALUPAS, Y ;
TAYLOR, AMKP ;
WHITELAW, JH .
PROCEEDINGS OF THE ROYAL SOCIETY OF LONDON SERIES A-MATHEMATICAL AND PHYSICAL SCIENCES, 1989, 426 (1870) :31-78