Transient gas-to-particle heat transfer measurements in a spouted bed

被引:32
作者
Brown, Steven L. [1 ]
Lattimer, Brian Y. [1 ]
机构
[1] Virginia Tech, Dept Mech Engn, Blacksburg, VA 24061 USA
关键词
Fluidization; Gas to particle; Infrared measurement; Particle temperature; Spouted bed; Transient heat transfer; SOLID FLUIDIZED-BED; MASS-TRANSFER; HYDRODYNAMICS; WALL; REACTOR;
D O I
10.1016/j.expthermflusci.2012.10.004
中图分类号
O414.1 [热力学];
学科分类号
摘要
Heat transfer characteristics of fluidized particles were experimentally quantified through measuring emitted infrared radiation. The presented experimental technique was designed to overcome the spatial, time varying, and instrumental intrusive limitations often found in multiphase flow studies. A pseudo two-dimensional bed was investigated by supplying a thermo-transient inlet gas temperature to fluidized, spouted, and fixed bed regimes. The highest rates of energy stored in the particles were found along the downward particulate entrainment zones surrounding the inlet gas channel. Gas-to-particle heat transfer coefficients in the spouted regime were computed per bed axial position. The resulting values found in the lower portion of the spout were in close comparison to the averaged gas-to-particle heat transfer coefficient empirical correlations found in literature. New findings are given on the high convective heat transfer coefficients in the spout fountain region, resulting from the highly turbulent nature of gas-solid mixing. (C) 2012 Elsevier Inc. All rights reserved.
引用
收藏
页码:883 / 892
页数:10
相关论文
共 25 条
[1]   Influence of multiple gas inlet jets on fluidized bed hydrodynamics using Particle Image Velocimetry and Digital Image Analysis [J].
Agarwal, Gaurav ;
Lattimer, Brian ;
Ekkad, Srinath ;
Vandsburger, Uri .
POWDER TECHNOLOGY, 2011, 214 (01) :122-134
[2]   SOME ASPECTS OF HEAT-TRANSFER BETWEEN A VERTICAL WALL AND A GAS FLUIDIZED-BED [J].
BAEYENS, J ;
GOOSSENS, WR .
POWDER TECHNOLOGY, 1973, 8 (1-2) :91-96
[3]  
Brown S., INT J MULTIPHA UNPUB
[4]   WALL-TO-BED HEAT-TRANSFER CHARACTERISTICS OF SPOUT-FLUID BEDS [J].
CHATTERJEE, A ;
ADUSUMILLI, RSS ;
DESHMUKH, AV .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1983, 61 (03) :390-397
[5]   MEASUREMENTS OF SPOUT VOIDAGE DISTRIBUTIONS, PARTICLE VELOCITIES AND PARTICLE CIRCULATION RATES IN SPOUTED BEDS OF COARSE PARTICLES .2. EXPERIMENTAL-VERIFICATION [J].
DAY, JY ;
MORGAN, MH ;
LITTMAN, H .
CHEMICAL ENGINEERING SCIENCE, 1987, 42 (06) :1461-1470
[6]   HEAT TRANSFER IN SPRAYED SPOUTED BEDS [J].
Englart, Sebastian ;
Kmiec, Andrzej ;
Ludwinska, Agnieszka .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2009, 87 (02) :185-192
[7]   HEAT AND MASS TRANSFER IN SPOUTED BEDS - REVIEW [J].
EPSTEIN, N ;
MATHUR, KB .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1971, 49 (04) :467-&
[8]   Heat transfer in a draft tube spouted bed with bottom solids feed [J].
Freitas, LAP ;
Freire, JT .
POWDER TECHNOLOGY, 2001, 114 (1-3) :152-162
[9]  
GUO Q, 1996, CHEM IND ENG, V13, P14
[10]   Experimental and Numerical Study of Hydrodynamics with Heat Transfer in a Gas-Solid Fluidized-Bed Reactor at Different Particle Sizes [J].
Hamzehei, Mahdi ;
Rahimzadeh, Tiassan .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2009, 48 (06) :3177-3186