SIMPLE METHOD FOR THE ESTIMATION OF FREE-FALL VELOCITY OF SPHERICAL-PARTICLES IN POWER LAW LIQUIDS

被引:24
作者
CHHABRA, RP
PERI, SS
机构
[1] Department of Chemical Engineering, Indian Institute of Technology, Kanpur
关键词
D O I
10.1016/0032-5910(91)80110-5
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Knowledge of the settling velocity of spherical particles in non-Newtonian power law liquids is required in design calculations for hydraulic conveying systems, using dense media, thickening and fluidization equipment, etc. In this work, an empirical formula has been developed which is explicit in velocity and reproduces a vast amount of data available in the literature. The scheme presented herein reproduces the results of nearly 400 individual sphere fall tests with an average error of 14% over wide ranges or rheological conditions and Reynolds numbers from 1 to 10(4).
引用
收藏
页码:287 / 290
页数:4
相关论文
共 24 条
[1]  
ACHARYA A, 1976, THESIS SALFORD U SAL
[2]  
Charles M. E., 1971, ADV SOLID LIQUID FLO, P187, DOI [10.1016/B978-0-08-015767-2.50015-6, DOI 10.1016/B978-0-08-015767-2.50015-6]
[3]  
Chhabra R.P., 1980, THESIS MONASH U MELB
[4]  
CHHABRA RP, 1985, CHEM ENG RES DES, V63, P390
[5]   WALL EFFECT FOR HIGH REYNOLDS-NUMBER MOTION OF SPHERES IN SHEAR THINNING FLUIDS [J].
CHHABRA, RP ;
UHLHERR, PHT .
CHEMICAL ENGINEERING COMMUNICATIONS, 1980, 5 (1-4) :115-124
[6]  
CHHABRA RP, 1977, 6TH P AUSTR HYDR FLU, P435
[7]   NON-NEWTONIAN VISCOSITY MEASUREMENTS IN THE INTERMEDIATE SHEAR RATE RANGE WITH THE FALLING-BALL VISCOMETER [J].
CHO, YI ;
HARTNETT, JP ;
LEE, WY .
JOURNAL OF NON-NEWTONIAN FLUID MECHANICS, 1984, 15 (01) :61-74
[8]  
Clift R., 1978, BUBBLES DROPS PARTIC
[9]  
DALLON DS, 1967, THESIS U UTAH SALT L
[10]  
DOLECEK P, 1983, CHISA