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Editorial

Editorial for Special Issue “Hydrodynamics and Gas Dispersion in Flotation”

1
Department of Chemical and Environmental Engineering, Universidad Técnica Federico Santa María, Valparaíso 2390123, Chile
2
COG Technologies Inc., Montréal, QC H3C 4L3, Canada
*
Author to whom correspondence should be addressed.
Minerals 2023, 13(9), 1219; https://doi.org/10.3390/min13091219
Submission received: 13 September 2023 / Accepted: 14 September 2023 / Published: 17 September 2023
(This article belongs to the Special Issue Hydrodynamics and Gas Dispersion in Flotation)
Gas dispersion, the breakage of a mass of gas into a population of small bubbles, is one of the most important subprocesses occurring in flotation machines. The technology establishes hydrodynamic conditions for the selective separation of particles via the formation and removal of bubble–particle aggregates. Flotation machines are designed and operated to provide a collection zone for the formation of bubble–particle aggregates, and a froth zone for the separation and concentration of these aggregates into a concentrate stream. Operators manipulate gas flow rate, pulp density, and frother concentration to maximize the available area of the bubble population. In addition, the froth depth and frother type are also defined to control the breakage rate of bubble–particle aggregates, as they rise to overflow into the concentrate launder. The variables used to characterize gas dispersion are the bubble size distribution (represented as an average diameter), gas holdup, superficial gas rate, and water carried by bubbles from the collection into the froth zone.
The eleven papers submitted to this Special Issue show the current interest of different research groups in improving metallurgical performance based on characterizing and better understanding machine hydrodynamics. There are four contributions on the development of online sensors, simulators, and models to define the machine designs and operating strategies: (i) a correlation between froth water content and water overflow rate [1], (ii) a correlation between gas holdup and flotation performance, which demonstrated that the former captured the combined effect of gas rate and frother concentration [2], (iii) a demonstration of a model reliability to predict bubble size from gas velocity and holdup measurements [3], and (iv) a simulation tool that incorporated gas dispersion, which proved the potential of changing the launder designs to improve flotation performances [4]. Bubble size measurement was another area with three contributions: the effect on interfacial area by considering stereological corrections in the bubble size estimation from 2D images [5], the increase in the automatically identified bubbles by modifying the sampling devices to reduce the presence of clusters [6], and the detection of abnormal hydrodynamic conditions (presence of cap-shaped bubbles) in industrial flotation machines [7]. An option for increasing the formation of bubble–particle aggregates is the use of micro and nanobubbles: a review on the generation, detection, and applications of nanobubbles in flotation was included in this volume [8], along with a study on the potential of bulk micro-nano-bubbles to improve quartz recovery [9]. The use of pulps containing soluble ions and frother molecules at the same time has been common in current flotation practice: (i) the arrangement of adsorbed frother molecules on the bubble surface proved to be influenced by the presence of different ions in the pulp [10], and (ii) electrolytes proved to reduce bubble coalescence, favoring the formation of small bubbles; however, in some conditions, they also promoted the formation by breakup, resulting in larger bubbles [11].
We appreciate the invitation extended by Minerals to organize this Special Issue. Special thanks go to all the authors for their time in preparing manuscripts, and also to the professionals that participated in the reviewing process.

Author Contributions

Conceptualization, C.O.G. and L.V.; methodology, C.O.G. and L.V.; software, C.O.G. and L.V.; validation, C.O.G. and L.V.; formal analysis, C.O.G. and L.V.; investigation, C.O.G. and L.V.; resources, C.O.G. and L.V.; data curation, C.O.G. and L.V.; writing—original draft preparation, C.O.G. and L.V.; writing—review and editing, C.O.G. and L.V.; visualization, C.O.G. and L.V.; supervision, C.O.G. and L.V.; project administration, C.O.G. and L.V.; funding acquisition, C.O.G. and L.V. All authors have read and agreed to the published version of the manuscript.

Conflicts of Interest

The authors declare no conflict of interest.

References

  1. Lepage, M.R.; Gomez, C.O.; Waters, K.E. Using Top-of-Froth Conductivity to Infer Water Overflow Rate in a Two-Phase Lab-Scale Flotation Column. Minerals 2022, 12, 454. [Google Scholar] [CrossRef]
  2. Femenias, F.; Maldonado, M.; Miranda, N.; Gutierrez, L. Flotation Performance and Gas Dispersion Properties in a Laboratory Flotation Cell. Minerals 2022, 12, 1351. [Google Scholar] [CrossRef]
  3. Gomez, C.O.; Maldonado, M. Modelling Bubble Flow Hydrodynamics: Drift-Flux and Molerus Models. Minerals 2022, 12, 1502. [Google Scholar] [CrossRef]
  4. Vallejos, P.; Yianatos, J.; Grau, R.; Yáñez, A. The Impact of Froth Launders Design in an Industrial Flotation Bank Using Novel Metallurgical and Hydrodynamic Models. Minerals 2023, 13, 169. [Google Scholar] [CrossRef]
  5. Vinnett, L.; Mesa, D. The Role of Stereological Assumptions in Bubble Size Estimations and Their Implications for Assessing Critical Coalescence Concentrations. Minerals 2023, 13, 803. [Google Scholar] [CrossRef]
  6. Vinnett, L.; Urriola, B.; Orellana, F.; Guajardo, C.; Esteban, A. Reducing the Presence of Clusters in Bubble Size Measurements for Gas Dispersion Characterizations. Minerals 2022, 12, 1148. [Google Scholar] [CrossRef]
  7. Vinnett, L.; Yianatos, J.; Acuña, C.; Cornejo, I. A Method to Detect Abnormal Gas Dispersion Conditions in Flotation Machines. Minerals 2022, 12, 125. [Google Scholar] [CrossRef]
  8. Nazari, S.; Hassanzadeh, A.; He, Y.; Khoshdast, H.; Kowalczuk, P.B. Recent Developments in Generation, Detection and Application of Nanobubbles in Flotation. Minerals 2022, 12, 462. [Google Scholar] [CrossRef]
  9. Zhou, S.; Li, Y.; Nazari, S.; Bu, X.; Hassanzadeh, A.; Ni, C.; He, Y.; Xie, G. An Assessment of the Role of Combined Bulk Micro- and Nano-Bubbles in Quartz Flotation. Minerals 2022, 12, 944. [Google Scholar] [CrossRef]
  10. Alvarado, O.; Quezada, G.R.; Saavedra, J.H.; Rozas, R.E.; Gutiérrez, L.; Toledo, P.G. Alkali Halide and MIBC Interaction at Typical Flotation Interfaces in Saline Water as Determined by Molecular Dynamics Simulations. Minerals 2023, 13, 665. [Google Scholar] [CrossRef]
  11. Chu, P.; Li, R.; Lepage, M.; Waters, K. Investigation of the Effect of Electrolytes on the Breakaway of Air Bubbles at an Underwater Capillary Using High-Speed Cinematography and Passive Acoustic Techniques. Minerals 2022, 12, 972. [Google Scholar] [CrossRef]
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MDPI and ACS Style

Vinnett, L.; Gómez, C.O. Editorial for Special Issue “Hydrodynamics and Gas Dispersion in Flotation”. Minerals 2023, 13, 1219. https://doi.org/10.3390/min13091219

AMA Style

Vinnett L, Gómez CO. Editorial for Special Issue “Hydrodynamics and Gas Dispersion in Flotation”. Minerals. 2023; 13(9):1219. https://doi.org/10.3390/min13091219

Chicago/Turabian Style

Vinnett, Luis, and César O. Gómez. 2023. "Editorial for Special Issue “Hydrodynamics and Gas Dispersion in Flotation”" Minerals 13, no. 9: 1219. https://doi.org/10.3390/min13091219

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