TRANSPORT PHENOMENA IN MULTI-PARTICLE SYSTEMS .2. PARTICLE-FLUID HEAT AND MASS-TRANSFER

被引:55
作者
AGARWAL, PK
机构
[1] Univ of Adelaide
关键词
Chemical Equipment - Fluidized Beds - Flow of Fluids - Mathematical Models - Heat Transfer - Mass Transfer;
D O I
10.1016/0009-2509(88)85184-4
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Particle-fluid heat/mass transfer in multi-particle systems is considered. The approach developed extends the model for momentum transfer reported in an earlier paper. Based on a boundary layer formulation for individual particles in the sphere assemblage, the model enables a unified, consideration of fixed, distended, fluidized beds as well as isolated spheres. A simple relationship between the heat/mass transfer characteristics and the hydrodynamics of multi-particle systems is obtained. The predictions of the model are compared with reported experimental data.
引用
收藏
页码:2501 / 2510
页数:10
相关论文
共 77 条
[1]   TRANSPORT PHENOMENA IN MULTI-PARTICLE SYSTEMS .1. PRESSURE-DROP AND FRICTION FACTORS - UNIFYING THE HYDRAULIC-RADIUS AND SUBMERGED-OBJECT APPROACHES [J].
AGARWAL, PK ;
ONEILL, BK .
CHEMICAL ENGINEERING SCIENCE, 1988, 43 (09) :2487-2499
[2]  
ANDERSSON KEB, 1961, CHEM ENG SCI, V15, P276
[3]  
ANDERSSON KEB, 1964, T R I TECHNOL STOCKH
[4]  
ANDERSSON KEB, 1963, T R I TECHNOL STOCKH
[5]   HEAT TRANSFER AND DIFFUSION IN FIXED BEDS [J].
ASBJORNSEN, OA ;
WANG, B .
CHEMICAL ENGINEERING SCIENCE, 1971, 26 (05) :585-+
[6]  
BRADSHAW AV, 1970, TRANS INST CHEM ENG, V48, pT77
[7]  
BROWN RAS, 1961, J CHEM ENG DATA, V6, P355
[8]   COMMENTS ON BUOYANCY IN FLUIDIZED-BEDS [J].
CLIFT, R ;
SEVILLE, JPK ;
MOORE, SC ;
CHAVARIE, C .
CHEMICAL ENGINEERING SCIENCE, 1987, 42 (01) :191-194
[9]  
Clift R., 1978, BUBBLES DROPS PARTIC
[10]  
CORNISH ARH, 1965, T I CHEM ENG-LOND, V43, P332