A flotation framework for Eulerian multiphase CFD: Integrating bubble-particle aggregates and flotation kinetics

被引:0
作者
Draw, Mazen [1 ,2 ]
Rzehak, Roland [1 ]
机构
[1] Helmholtz Zentrum Dresden Rossendorf, Inst Fluid Dynam, Bautzner Landstr 400, D-01328 Dresden, Germany
[2] Tech Univ Dresden, Inst Proc Engn & Environm Technol, D-01069 Dresden, Germany
关键词
Flotation; Bubble-particle aggregates; Attachment and detachment kinetics; Aggregate density; Eulerian multi-fluid model; CFD simulation; FLOW; SIMULATION; COLUMNS; MODEL; COLLISION; DROPS; DRAG;
D O I
10.1016/j.mineng.2025.109258
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Flotation is a key process for the beneficiation of raw materials in mineral engineering involving complex multiphase flows. The Eulerian multi-fluid approach enables the simulation of such flows up to industrial scales by treating all phases as interpenetrating continua. For flotation, one phase consists of aggregates of a bubble and attached particles. The formation of these aggregates is governed by the kinetics of bubble-particle attachment and detachment. Their buoyancy depends on the attached particles and differs from that of unloaded bubbles. The present work extends a flotation framework to account for these phenomena by considering the aggregates as a multicomponent phase of a floatable particle- and an inert bubble-species. Methods for reactive mass transfer available in major CFD codes can then be adapted to describe the flotation kinetics. Demonstration cases with simplified and realistic attachment models are shown to verify the implementation of the framework in OpenFOAM and illustrate possible uses for flotation.
引用
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页数:13
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