Detachment of particles from bubbles in an agitated vessel

被引:73
作者
Goel, Shina [1 ]
Jameson, Graeme J. [1 ]
机构
[1] Univ Newcastle, Ctr Multiphase Proc, Callaghan, NSW 2308, Australia
基金
澳大利亚研究理事会;
关键词
Coarse particle flotation; Bond number; Particle detachment; SIZE; FLOTATION; TURBULENCE;
D O I
10.1016/j.mineng.2012.08.001
中图分类号
TQ [化学工业];
学科分类号
081705 [工业催化];
摘要
The flotation process is widely used to separate valuable minerals from waste in the minerals industry. It is well known that recovery decreases with increasing particle size, and a reason often given is that large particles detach from bubbles in the turbulent shear flow induced by the impeller in mechanical flotation cells. The energy produced by the impeller is transferred to the liquid in the cell and dissipates throughout the tank. In the impeller region, the turbulence is non-isotropic, but in a very short distance, it becomes isotropic, with the typical cascade of eddies from large to micro-scale length scales. The aim of this study is to observe the behavior of particle-laden bubbles in the turbulent shear flow near a rotating impeller in a flotation cell. An agitated vessel was constructed in which bubbles could be introduced beneath the impeller. Bubbles were generated in a liquid-fluidized bed in a special chamber beneath the cell, in which the fluidizing liquid contained a collector that enabled the particles in the bed to adhere to the bubbles. When the bubbles entered the impeller zone, some particles were observed to detach, while others remained attached to the bubble and rose out of the vessel as a flotation product. The fractional detachment of particles was related to the mechanical energy dissipation rate in the region of the impeller. A standard Rushton turbine was used. The results are compared with theoretical predictions of Schulze (1977, 1982). (C) 2012 Elsevier Ltd. All rights reserved.
引用
收藏
页码:324 / 330
页数:7
相关论文
共 23 条
[1]
THE EFFECT OF BUBBLE-SIZE ON THE RATE OF FLOTATION OF FINE PARTICLES [J].
AHMED, N ;
JAMESON, GJ .
INTERNATIONAL JOURNAL OF MINERAL PROCESSING, 1985, 14 (03) :195-215
[2]
On the breakup of fluid particles in turbulent flows [J].
Andersson, R ;
Andersson, B .
AICHE JOURNAL, 2006, 52 (06) :2020-2030
[3]
Analysis of turbulence anisotropy in a mixing tank [J].
Escudié, R ;
Liné, A .
CHEMICAL ENGINEERING SCIENCE, 2006, 61 (09) :2771-2779
[4]
Evaluation of local kinetic energy dissipation rate in the impeller stream of a Rushton turbine by time-resolved PIV [J].
Huchet, F. ;
Line, A. ;
Morchain, J. .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2009, 87 (4A) :369-376
[5]
JAMESON GJ, 1977, MINER SCI ENG, V9, P103
[6]
New directions in flotation machine design [J].
Jameson, Graeme J. .
MINERALS ENGINEERING, 2010, 23 (11-13) :835-841
[7]
Jowett A., 1980, Fine Particles Processing, 1, P720
[8]
Kolmogoroff AN, 1941, CR ACAD SCI URSS, V32, P16
[9]
PREDICTION OF THE 3-DIMENSIONAL TURBULENT-FLOW IN STIRRED TANKS [J].
KRESTA, SM ;
WOOD, PE .
AICHE JOURNAL, 1991, 37 (03) :448-460
[10]
Turbulence properties of the impeller stream of a Rushton turbine [J].
Lee, KC ;
Yianneskis, M .
AICHE JOURNAL, 1998, 44 (01) :13-24