TRANSPORT PHENOMENA IN MULTI-PARTICLE SYSTEMS .1. PRESSURE-DROP AND FRICTION FACTORS - UNIFYING THE HYDRAULIC-RADIUS AND SUBMERGED-OBJECT APPROACHES

被引:33
作者
AGARWAL, PK
ONEILL, BK
机构
[1] Univ of Adelaide
关键词
Chemical Equipment - Fluidized Beds - Flow of Fluids - Mathematical Models;
D O I
10.1016/0009-2509(88)85183-2
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A submerged-object model which accounts for the presence of stagnant zones is developed for predicting the pressure drop in random multi-particle systems. This model is then combined with the hydraulic-radius approach. With appropriate definition of the parameters involved, these approaches are found to yield complementary results. The approach, in principle, permits the collapsing of the entire momentum transfer data for multi-particle systems to a single curve coincident with the single-sphere drag coefficient relation. Friction factors calculated from the experimental data reported in the literature on packed, fluidized and distended beds, as well as sedimenting systems, are in good agreement with the theory for laminar as well as turbulent regimes. An expression for the relative velocity of sedimenting suspensions, applicable to a wide range of Reynolds number and void fractions, is obtained. An approximation for the estimation of the minimum fluidizing velocity is also developed and compared with the data available in the literature.
引用
收藏
页码:2487 / 2499
页数:13
相关论文
共 58 条
[11]  
Clift R., 1978, BUBBLES DROPS PARTIC
[12]  
Couderc J. P., 1985, FLUIDIZATION, P1
[13]  
ERGUN S, 1952, CHEM ENG PROG, V48, P89
[14]   ON THE DRAG COEFFICIENT OF A SPHERE [J].
FLEMMER, RLC ;
BANKS, CL .
POWDER TECHNOLOGY, 1986, 48 (03) :217-221
[15]   A UNIFIED MODEL FOR PARTICULATE EXPANSION OF FLUIDIZED-BEDS AND FLOW IN FIXED POROUS-MEDIA [J].
FOSCOLO, PU ;
GIBILARO, LG ;
WALDRAM, SP .
CHEMICAL ENGINEERING SCIENCE, 1983, 38 (08) :1251-1260
[16]   A MODEL OF MECHANISM OF TRANSPORT IN PACKED, DISTENDED, AND FLUIDIZED BEDS [J].
GALLOWAY, TR ;
SAGE, BH .
CHEMICAL ENGINEERING SCIENCE, 1970, 25 (03) :495-&
[17]   VELOCITY-VOIDAGE RELATIONSHIPS FOR FLUIDIZATION AND SEDIMENTATION IN SOLID-LIQUID SYSTEMS [J].
GARSIDE, J ;
ALDIBOUNI, MR .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1977, 16 (02) :206-214
[18]   MOMENTUM-TRANSFER THROUGH PACKED-BEDS OF VARIOUS PARTICLES IN TURBULENT-FLOW REGIME [J].
GAUVIN, WH ;
KATTA, S .
AICHE JOURNAL, 1973, 19 (04) :775-783
[19]   A PAIRWISE ADDITIVE DESCRIPTION OF SEDIMENTATION AND DIFFUSION IN CONCENTRATED SUSPENSIONS OF HARD-SPHERES [J].
GLENDINNING, AB ;
RUSSEL, WB .
JOURNAL OF COLLOID AND INTERFACE SCIENCE, 1982, 89 (01) :124-143
[20]   COMPARISON OF COMMONLY USED CORRELATIONS FOR MINIMUM FLUIDIZATION VELOCITY OF SMALL SOLID PARTICLES [J].
GREWAL, NS ;
SAXENA, SC .
POWDER TECHNOLOGY, 1980, 26 (02) :229-234