Improving coarse particle flotation using the HydroFloat™ (raising the trunk of the elephant curve)

被引:67
作者
Kohmuench, J. N. [1 ]
Mankosa, M. J. [2 ]
Thanasekaran, H. [1 ]
Hobert, A. [2 ]
机构
[1] Eries Magnet Pty Ltd, 21 Shirley Way, Epping, Vic 3076, Australia
[2] Eries Mfg Co, 2200 Asbury Rd, Erie, PA 16506 USA
关键词
Coarse particle flotation; Fluidized bed flotation; Sulfide flotation; HydroFloat;
D O I
10.1016/j.mineng.2018.03.004
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The copper sulfide processing flowsheet has remained virtually untouched for decades and follows a logical progression - crush, grind, float, regrind and refloat to produce a final copper concentrate. This well-defined and proven method of copper sulfide processing has served the industry well for over a century and is based on the particle size range for which conventional flotation is most effective. Work by numerous experts has shown that mechanical flotation works well for a limited size range, from approximately 15 to 150 pm, and is best presented in the well-recognized "elephant curve." Particles outside this critical size range are typically lost in industrial operations and rejected to tailings due to inherent constraints associated with the physical interactions that occur in the pulp and froth phases of conventional flotation equipment. The underlying mechanisms responsible for the decline in flotation recovery of very fine and very coarse particles have been extensively discussed in the technical literature. For coarser particles, low recovery is typically attributed to both turbulence and buoyancy constraints. To overcome these inherent limitations found in conventional flotation cells, Eriez has developed and successfully implemented a technology, the HydroFloat'', that combines the aspects of fluidized-bed separation and flotation. More recently, this same technology has been demonstrated in sulfides for recovering coarse value from concentrator tails. Other efforts have shown the positive benefit that can be derived from implementation within the concentrator itself. This paper will discuss the theory of operation of fluidized-bed flotation and data from various applications are presented.
引用
收藏
页码:137 / 145
页数:9
相关论文
共 27 条
  • [1] Arbiter N., 1962, Froth Flotation, P215
  • [2] Ata S., 2009, SME ANN M 2009 SOC M
  • [3] Incorporating fluidised-bed flotation into a conventional flotation flowsheet: A focus on energy implications of coarse particle recovery
    Awatey, Bellson
    Skinner, William
    Zanin, Massimiliano
    [J]. POWDER TECHNOLOGY, 2015, 275 : 85 - 93
  • [4] Optimization of operating parameters for coarse sphalerite flotation in the Hydro Float fluidised-bed separator
    Awatey, Bellson
    Thanasekaran, Homie
    Kohmuench, Jaisen N.
    Skinner, William
    Zanin, Massimiliano
    [J]. MINERALS ENGINEERING, 2013, 50-51 : 99 - 105
  • [5] Barbery G., 1984, SCI BASIS FLOTATION, P289
  • [6] Barbery G., 1989, US Patent, Patent No. [4,822,493, 4822493]
  • [7] Flotation of coarse composite particles in mechanical cell vs. the fluidised-bed separator (The HydroFloat™)
    Fosu, Shadrack
    Awatey, Bellson
    Skinner, William
    Zanin, Massimiliano
    [J]. MINERALS ENGINEERING, 2015, 77 : 137 - 149
  • [8] Gaudin A, 1931, TECHNICAL PUBLICATIO
  • [9] Jameson G. H., 2007, PCT Patent, Patent No. [200810422A1, 200810422]
  • [10] Jameson G.J, 2014, 27 INT MIN PROC C SA