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A Review of Flotation Physical Froth Flow Modifiers

Journal

MINERALS
Volume 11, Issue 8, Pages -

Publisher

MDPI
DOI: 10.3390/min11080864

Keywords

froth stability; froth phase sub-processes; froth retention time; physical froth flow modifiers; froth carry rate; froth crowders; launders

Funding

  1. Institute for Development of Energy for African Sustainability (IDEAS) at the University of South Africa (UNISA) [120392]
  2. NRF (National Research Foundation)

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The increase in size of flotation cells has posed challenges in froth removal in industrial operations, leading to the use of physical froth flow modifiers to improve froth drainage and flow dynamics. While certain modifiers like crowders and launders are widely utilized, others like froth baffles and scrapers have limited industrial uptake. Further research is needed to understand the impact of physical modifiers on particle selectivity.
Over the past few decades, the need to process more minerals while lowering capital costs has led to an increase in the size of flotation cells, e.g., 0.03 m(3) to 1000 m(3). However, this increase has created new challenges in the operation and design of industrial flotation cells, particularly in terms of froth removal, because the distance the froth must travel increases with an increase in the flotation cell diameter. This has a negative impact on recovery. Physical froth flow modifiers can be used to improve froth removal. Their major functions are to modify and optimise the flow of the froth, improve froth drainage, reduce dead zones, and improve froth flow and removal dynamics. Therefore, physical froth flow modifiers are discussed, evaluated, and compared in this paper. The literature indicates that physical froth flow modifiers such as crowders and launders are used extensively as industrial solutions to enhance froth transport and recovery in large flotation cells. Other modifiers (including froth baffles and froth scrapers) have been found to have a profound effect on local froth phase sub-processes, including drainage and bubble coalescence. However, industrial uptake is either dwindling or limited to small-volume rectangular/U-shaped cells in the case of scrapers, or, there is no uptake at all in the case of froth baffles. Further research on how some of the physical modifiers (e.g., baffles and launders) impact the selectivity of particles is required.

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