Particle motion in L-valve as observed by positron emission particle tracking

被引:30
作者
Chan, Chian W. [1 ]
Seville, Jonathan [1 ]
Fan, Xianfeng [2 ]
Baeyens, Jan [1 ,3 ]
机构
[1] Univ Warwick, Sch Engn, Coventry CV4 7AL, W Midlands, England
[2] Univ Birmingham, Sch Phys & Astron, Birmingham B15 2TT, W Midlands, England
[3] UCL, Dept Chem Engn, London WC1E 7HB, England
关键词
Positron emission particle tracking (PEPT); L-valve; Circulating fluidised bed; Tracer; Positron tracking; Dune flow; SINGLE-PARTICLE; SOLIDS FLOW; BEHAVIOR;
D O I
10.1016/j.powtec.2009.02.016
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
L-valves are widely used in circulating fluidized beds (CFB) to control the solid circulation rate. Positron emission particle tracking (PEPT) is used to view and study the real-time particle motion in the L-valve. The paper presents experimental results of the solid motion and solid flux in the L-valve, G, as a function of the superficial injection air velocity, U. Results are compared with earlier work. The size of the L-valve is 4.5 cm I.D. Two different experimental configurations (L-valve discharge in a CFB riser and free discharge) were used. The L-valve flow regime is stable until approximately 6 U/U(mf), with proportionality between solid flux and U/U(mf). At a higher U/U(mf),unsteady fluctuations in the solid flow gradually increase due to cavity formation around the L-valve elbow. Increasing the air flow even further, a maximum flow is reached, corresponding to the maximum discharge rate through the cyclone or hopper apex. PEPT has also confirmed the existence of a dune flow. For the first time, it gives quantitative data of the velocity profile of the dune flow which is governed by two important factors. The first factor is the distance of solids from the base of the L-valve, with solid velocity increasing away from the base. The second factor is the location of solids with respect to the dune, i.e. solid velocity is minimum at the base of the dunes and maximum at the top of the duties. The average voidage in the L-valve is approximately constant and independent of U. (C) 2009 Elsevier B.V.. All rights reserved.
引用
收藏
页码:137 / 149
页数:13
相关论文
共 24 条
[1]   L-valve behaviour with solids of different size and density [J].
Arena, U ;
Langeli, CB ;
Cammarota, A .
POWDER TECHNOLOGY, 1998, 98 (03) :231-240
[2]   THE FLOW OF GRANULAR SOLIDS THROUGH ORIFICES [J].
BEVERLOO, WA ;
LENIGER, HA ;
VANDEVELDE, J .
CHEMICAL ENGINEERING SCIENCE, 1961, 15 (3-4) :260-&
[3]   EFFECT OF FLUID-DRAG FORCES ON DISCHARGE OF FREE-FLOWING SOLIDS FROM HOPPERS [J].
CARLETON, AJ .
POWDER TECHNOLOGY, 1972, 6 (02) :91-&
[4]  
CHAN CW, 2008, P CIRCULATING FLUIDI, V9, P981
[5]  
CHAN CW, IEC R IN PRESS
[6]   Modeling solids and gas flow through an L-valve [J].
Daous, MA ;
Al-Zahrani, AA .
POWDER TECHNOLOGY, 1998, 99 (01) :86-89
[7]   Labelling a single particle for positron emission particle tracking using direct activation and ion-exchange techniques [J].
Fan, X. ;
Parker, D. J. ;
Smith, M. D. .
NUCLEAR INSTRUMENTS & METHODS IN PHYSICS RESEARCH SECTION A-ACCELERATORS SPECTROMETERS DETECTORS AND ASSOCIATED EQUIPMENT, 2006, 562 (01) :345-350
[8]   Enhancing 18F uptake in a single particle for positron emission particle tracking through modification of solid surface chemistry [J].
Fan, X ;
Parker, DJ ;
Smith, MD .
NUCLEAR INSTRUMENTS & METHODS IN PHYSICS RESEARCH SECTION A-ACCELERATORS SPECTROMETERS DETECTORS AND ASSOCIATED EQUIPMENT, 2006, 558 (02) :542-546
[9]   THE BEHAVIOR OF L-VALVES WITH GRANULAR POWDERS [J].
GELDART, D ;
JONES, P .
POWDER TECHNOLOGY, 1991, 67 (02) :163-174
[10]   Effects of solids feeder and riser exit configuration on establishing high density circulating fluidized beds [J].
Kim, Jun-Sik ;
Tachino, Ryo ;
Tsutsumi, Atsushi .
POWDER TECHNOLOGY, 2008, 187 (01) :37-45