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Canadian Metallurgical Quarterly
The Canadian Journal of Metallurgy and Materials Science
Volume 62, 2023 - Issue 3
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Mineral Processing

Temperature and climate-induced fluctuations in froth flotation: an overview of different ore types

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Pages 511-548 | Received 14 Jul 2022, Accepted 18 Sep 2022, Published online: 30 Sep 2022

Figures & data

Table 1. Summary of reagents mentioned in literature.

Figure 1. Examples of seasonal drop: (a) in gold recovery on Hudson Bay Mining and Smelting, 2000–2003; (b) in Cu + Ni grade on Clarabelle mill, adapted from Refs. [Citation28,Citation63].

Figure 1. Examples of seasonal drop: (a) in gold recovery on Hudson Bay Mining and Smelting, 2000–2003; (b) in Cu + Ni grade on Clarabelle mill, adapted from Refs. [Citation28,Citation63].

Figure 2. (a) DO solubility in distilled water at different temperatures, adapted from Ref. [Citation90]; (b) effect of temperature on water viscosity and bubble size, adapted from Ref. [Citation91].

Figure 2. (a) DO solubility in distilled water at different temperatures, adapted from Ref. [Citation90]; (b) effect of temperature on water viscosity and bubble size, adapted from Ref. [Citation91].

Figure 3. Zinc concentrate grade fluctuations at Matagami concentrator, adapted from Ref. [Citation64].

Figure 3. Zinc concentrate grade fluctuations at Matagami concentrator, adapted from Ref. [Citation64].

Figure 4. Monthly pyrite production on a flotation plant in South Africa in relation to the temperature, adapted from [Citation66].

Figure 4. Monthly pyrite production on a flotation plant in South Africa in relation to the temperature, adapted from [Citation66].

Figure 5. (a) Concentrate quality depends on froth rheological properties; (b) changes in water and pyrite pulp viscosities, and water surface tension as a function of temperature. Adapted from Refs. [Citation66,Citation92].

Figure 5. (a) Concentrate quality depends on froth rheological properties; (b) changes in water and pyrite pulp viscosities, and water surface tension as a function of temperature. Adapted from Refs. [Citation66,Citation92].

Figure 6. Flotation recovery of selected sulphide minerals in relation to liquid-vapour surface tension, adapted from Ref. [Citation111].

Figure 6. Flotation recovery of selected sulphide minerals in relation to liquid-vapour surface tension, adapted from Ref. [Citation111].

Figure 7. Laboratory results of zinc rougher flotation, adapted from Ref. [Citation128].

Figure 7. Laboratory results of zinc rougher flotation, adapted from Ref. [Citation128].

Figure 8. Zinc recovery at the Neves-Corvo zinc plant in relation to the daily temperature, adapted from Ref. [Citation132].

Figure 8. Zinc recovery at the Neves-Corvo zinc plant in relation to the daily temperature, adapted from Ref. [Citation132].

Figure 9. Interaction scheme of xanthates with sulphide surface in aerated pulp, adapted from Ref. [Citation140], where Ev is the location of the energy level of the valence band ‘ceiling’, and Ec is the location of the energy level of the conductivity band ‘bottom’.

Figure 9. Interaction scheme of xanthates with sulphide surface in aerated pulp, adapted from Ref. [Citation140], where Ev is the location of the energy level of the valence band ‘ceiling’, and Ec is the location of the energy level of the conductivity band ‘bottom’.

Figure 10. (a) Butyl xanthate adsorption on pyritic surface, adapted from Ref. [Citation32]; (b) change of butyl xanthate concentration in the pulp (Ct/C0) with time during adsorption onto chalcopyrite, adapted from Ref. [Citation145].

Figure 10. (a) Butyl xanthate adsorption on pyritic surface, adapted from Ref. [Citation32]; (b) change of butyl xanthate concentration in the pulp (Ct/C0) with time during adsorption onto chalcopyrite, adapted from Ref. [Citation145].

Figure 11. Areas of pH and concentration stabilities of copper species at different temperatures, adapted from Ref. [Citation86].

Figure 11. Areas of pH and concentration stabilities of copper species at different temperatures, adapted from Ref. [Citation86].

Figure 12. Critical cyanide concentrations in captive bubble tests for combinations of activator and collector at different pH and under varying temperature conditions: (a) chalcopyrite (25 mg L−1 KEX), (b) sphalerite (150 mg L−1 Cu-vitriol), (c) pyrite, adapted from Ref. [Citation34].

Figure 12. Critical cyanide concentrations in captive bubble tests for combinations of activator and collector at different pH and under varying temperature conditions: (a) chalcopyrite (25 mg L−1 KEX), (b) sphalerite (150 mg L−1 Cu-vitriol), (c) pyrite, adapted from Ref. [Citation34].

Figure 13. A summary of some seasonality triggering mechanisms on sulphide flotation plants.

Figure 13. A summary of some seasonality triggering mechanisms on sulphide flotation plants.

Figure 14. Schematic representation of PNIPAM haematite flotation steps, with results compared with sodium oleate flotation, adapted from Ref. [Citation37].

Figure 14. Schematic representation of PNIPAM haematite flotation steps, with results compared with sodium oleate flotation, adapted from Ref. [Citation37].

Figure 15. Seasonal variations of niobium recovery at Niobec facilities, adapted from Ref. [Citation62]: months with negative recovery shift have blue bars, with positive shift having red bars, months with close to zero shift (<1%) have yellow bars or no bars. The zero point is mean summer recovery.

Figure 15. Seasonal variations of niobium recovery at Niobec facilities, adapted from Ref. [Citation62]: months with negative recovery shift have blue bars, with positive shift having red bars, months with close to zero shift (<1%) have yellow bars or no bars. The zero point is mean summer recovery.

Figure 16. Effect of flotation temperature on fluorite grade and recovery at pH 9 with oleic acid, adapted from [Citation188].

Figure 16. Effect of flotation temperature on fluorite grade and recovery at pH 9 with oleic acid, adapted from [Citation188].

Figure 17. Fluorite recovery as a function of pulp temperature and collector type, adapted from Ref. [Citation47].

Figure 17. Fluorite recovery as a function of pulp temperature and collector type, adapted from Ref. [Citation47].

Figure 18. Comparison of the composition of a commercial fatty acid collector and EV-1, plotted using data from Ref. [Citation50].

Figure 18. Comparison of the composition of a commercial fatty acid collector and EV-1, plotted using data from Ref. [Citation50].

Figure 19. Solubility surfaces for (a) halite and (b) sylvite as a function of MgCl2 and temperature (in a system with NaCl:KCl ratio of 1:1), adapted from Ref. [Citation206].

Figure 19. Solubility surfaces for (a) halite and (b) sylvite as a function of MgCl2 and temperature (in a system with NaCl:KCl ratio of 1:1), adapted from Ref. [Citation206].

Figure 20. Recovery and grade of lithium concentrate at different temperatures of the flotation pulp, adapted from Ref. [Citation237].

Figure 20. Recovery and grade of lithium concentrate at different temperatures of the flotation pulp, adapted from Ref. [Citation237].

Table 2. Summary of some reported optimal flotation temperatures for different minerals.

Figure 21. A concept of ‘flotation rectangular’ demonstrates seasonal triggers sphere of influence and flotation system components interactions.

Figure 21. A concept of ‘flotation rectangular’ demonstrates seasonal triggers sphere of influence and flotation system components interactions.