Rapid determination of non-Newtonian flow behavior in mineral suspensions

被引:1
|
作者
Bakshi, AK
Kawatra, SK
机构
[1] MICHIGAN TECHNOL UNIV, DEPT MET & MAT ENGN, HOUGHTON, MI 49931 USA
[2] MICHIGAN TECHNOL UNIV, DEPT MET & MAT ENGN, HOUGHTON, MI 49931 USA
关键词
D O I
10.1007/BF03402740
中图分类号
TF [冶金工业];
学科分类号
0806 ;
摘要
Mineral suspensions in water show Newtonian flow properties at low percent solids. However, this changes to a non-Newtonian regime as the percent solids increases. For Newtonian fluids, viscosity is independent of shear rate, but, for non-Newtonian fluids, viscosity varies with shear rate. Therefore, if the slurry is non-Newtonian, attempting to measure the viscosity at a shear rate different from the shear rate experienced by the fluid within the process is futile. This is especially true for a hydrocyclone, where the rate of shear is different at different points within the hydrocyclone. In this case, it is very important to determine the flow type of the suspension before attempting to establish any correlation between the viscosity and the process efficiency. A new technique to distinguish such changes inflow type was del eloped. This involves two viscometers: a coaxial cylinder-type viscometer that measures apparent viscosity at low shear rates and a vibrating sphere-type viscometer that measures the apparent viscosity at high shear rates. For each of these instruments, special precautions were taken to allow for the measurement of the viscosity of rapidly settling mineral suspensions. Because the vibrating sphere viscometer is operated at a much higher shear rate than the rotating viscometer, the two instruments together could determine the shear-rate dependency of the viscosity. Ground silica (80% passing 65 mu m) in water. was used to prepare slurries at concentrations ranging from 10% to 70% (by weight) solids. The viscosity of each slurry sample was measured simultaneously by both viscometers, and the results were compared. With this technique, it was found that all of the silica-slurry samples tested were in the Newtonian flow regime for up to 70% (by weight) solids. Methocel and Cellosize polymer solutions showed clear non-Newtonian behavior using this technique. This confirmed that non-Newtonian behavior of the silica slurries, if present, would have been detected by this arrangement.
引用
收藏
页码:165 / 169
页数:5
相关论文
共 50 条
  • [1] ON THE NON-NEWTONIAN BEHAVIOR OF SUSPENSIONS
    DECINDIO, B
    NICODEMO, L
    MASI, P
    RHEOLOGICA ACTA, 1987, 26 (01) : 100 - 101
  • [2] NON-NEWTONIAN BEHAVIOR OF SUSPENSIONS
    GARCIAFRANCO, CA
    ACTA MECHANICA, 1980, 37 (1-2) : 85 - 97
  • [3] Non-Newtonian flow behavior of suspensions of small sedimenting particles
    Werner, Franz
    Mersmann, Alfons
    Chemie-Ingenieur-Technik, 1995, 67 (03): : 317 - 320
  • [4] NON-NEWTONIAN BEHAVIOR OF FLOCCULATED SUSPENSIONS
    MILLS, P
    JOURNAL DE PHYSIQUE LETTRES, 1985, 46 (07): : L301 - L309
  • [5] NON-NEWTONIAN BEHAVIOR OF YEAST SUSPENSIONS
    ELTEMTAMY, S
    FARAHAT, L
    ELDIN, AN
    GABER, A
    EUROPEAN JOURNAL OF APPLIED MICROBIOLOGY AND BIOTECHNOLOGY, 1982, 15 (03): : 156 - 160
  • [6] NON-NEWTONIAN BEHAVIOR OF BROWNIAN PARTICLE SUSPENSIONS
    MILLS, P
    SNABRE, P
    QUEMADA, D
    REVUE DE PHYSIQUE APPLIQUEE, 1981, 16 (09): : 523 - 527
  • [7] INTERACTING FLOW-UNITS MODEL FOR NON-NEWTONIAN BEHAVIOR OF COLLOIDAL SUSPENSIONS
    PENDSE, H
    GREENLAW, FW
    JOURNAL OF RHEOLOGY, 1982, 26 (06) : 582 - 582
  • [8] Effects of non-Newtonian mineral suspensions on the performance of centrifugal pumps
    Sellgren, Anders
    Addie, Graeme
    Yu, Wei-Chung
    Mineral Processing and Extractive Metallurgy Review, 2000, 20 (01): : 239 - 249
  • [9] A MECHANISM FOR NON-NEWTONIAN FLOW IN SUSPENSIONS OF RIGID SPHERES
    KRIEGER, IM
    DOUGHERTY, TJ
    TRANSACTIONS OF THE SOCIETY OF RHEOLOGY, 1959, 3 : 137 - 152
  • [10] STEADY UNIFORM-FLOW OF NON-NEWTONIAN SUSPENSIONS
    IPPOLITO, M
    RHEOLOGICA ACTA, 1975, 14 (02) : 195 - 195