Abstract

After more than a century applying flotation to the mining industry, two completely different strategies have been introduced for processing purposes. One is the classical approach viz. grinding the ores to a certain extent and floating them via conventional mechanical and recently pneumatic cells e.g. Jameson and ImhoflotTM cells. This strategy continuous because mines face up to declining cut-off grades, complex and poly-mineralized ores, and they require to achieve an acceptable degree of mineral liberation. The other school of mind deals with the coarse particle processes mainly owing to the low energy needs, that includes flash, fluidized bed and HydroFloatTM cells. The third and newest system proposes processing both fine and coarse sizes by flotation machines like oscillating grid flotation (OGC) and Reflux flotation cells. The present paper endeavours to critically evaluate these concepts from several points of view including existing technological elaborations, water and energy usages, kinetics and circuit design. Brief introduction of advanced technologies, along with their applications, were presented. It was revealed that the incorporation of coarse grinding apparatuses, mineralogical techniques together with the technologically applicable classification systems and adapted simulator tools are urgent needs for coarse flotation as the future requirements for mining industries. However, fine particle flotation may remain as the main focus of re-processing tailings dams.

Highlights

  • Froth flotation was undoubtedly the most innovative and mining saver in ore dressing in the 19th century [1]

  • The idea is that it would be part of a split circuit, presorted into coarse and fine, with technologies tailored to each. To float both size ranges, the following sections exemplify two vessels developed in bench-scale including oscillating grid cell (OGC) and reflux flotation cell (RFC). 3.3.1

  • This study clearly demonstrates that optimal energy inputs for the flotation of fine and coarse particles differ significantly

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Summary

Introduction

Froth flotation was undoubtedly the most innovative and mining saver in ore dressing in the 19th century [1]. Three key points force the mining industries to coarse particle treatment containing I) drastic environmental consequences of wet tailings dams and acid mining drainage (AMD), II) losing precious materials in the coarse fraction sizes and III) enormous energy consumption (i.e., 2-4% global electricity usage) in comminution stages with less than 2% efficiency [4]. These concepts are well established, only a few technological developments have been appeared in mineral processing industries over the last decades. According to the raised assertions, there is an urgent need to tackle these issues related to either coarse or fine process mineralogies

Fine or coarse particulate systems
Findings
Conclusions
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