Abstract

Experimental assays and mathematical models, through population balance models (PBM), were used to characterize the particle aggregation of mining tailings flocculated in seawater. Three systems were considered for preparation of the slurries: i) Seawater at natural pH (pH 7.4), ii) seawater at pH 11, and iii) treated seawater at pH 11. The treated seawater had a reduced magnesium content in order to avoid the formation of solid complexes, which damage the concentration operations. For this, the pH of seawater was raised with lime before being used in the process—generating solid precipitates of magnesium that were removed by vacuum filtration. The mean size of the aggregates were represented by the mean chord length obtained with the Focused beam reflectance measurement (FBRM) technique, and their descriptions, obtained by the PBM, showed an aggregation and a breakage kernel had evolved. The fractal dimension and permeability were included in the model in order to improve the representation of the irregular structure of the aggregates. Then, five parameters were optimized: Three for the aggregation kernel and two for the breakage kernel. The results show that raising the pH from 8 to 11 was severely detrimental to the flocculation performance. Nevertheless, for pH 11, the aggregates slightly exceeded 100 µm, causing undesirable behaviour during the thickening operations. Interestingly, magnesium removal provided a suitable environment to perform the tailings flocculation at alkaline pH, making aggregates with sizes that exceeded 300 µm. Only the fractal dimension changed between pH 8 and treated seawater at pH 11—as reflected in the permeability outcomes. The PBM fitted well with the experimental data, and the parameters showed that the aggregation kernel was dominant at all-polymer dosages. The descriptive capacity of the model might have been utilized as a support in practical decisions regarding the best-operating requirements in the flocculation of copper tailings and water clarification.

Highlights

  • High-salinity resources, such as seawater, are being used in the mining industry in countries such as Australia, Chile, and Indonesia

  • The outcomes of this work are of particular interest to mining industries that use seawater in concentration stages, and the implementation of this plan might allow for sustainable have proven that, for these flocculated systems, it is possible to use a constant fractal dimension when results without the need to totally remove seawater salts by reverse osmosis

  • The population balance model (PBM) equations used in this work are derived from several works [42,43,44] that discretize the aggregate size into the number i of the bins

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Summary

Introduction

High-salinity resources, such as seawater, are being used in the mining industry in countries such as Australia, Chile, and Indonesia. The outcomes of this work are of particular interest to mining industries that use seawater in concentration stages, and the implementation of this plan might allow for sustainable have proven that, for these flocculated systems, it is possible to use a constant fractal dimension when results without the need to totally remove seawater salts by reverse osmosis. The seawater (SW) was obtained from the San Jorge Bay in Antofagasta (Chile); to eliminate of this work are of particular interest to mining industries that use seawater in concentration stages, bacterial activity, the SW was filtered at 1 μm using a UV filter system This water had a conductivity and the implementation of this plan might allow for sustainable results without the need to totally of 50.4 mS/cm, while its ionic composition was the following: 10.9 g/L Na+, 1.38 g/L Mg2+, 0.4 g/L Ca2+, remove seawater salts by reverse osmosis. The reagents used to modify the pH were lime and sodium hydroxide and were of analytical grade (greater than 98%)

Magnesium Removal
Flocculant-Suspension
L30 min using
Batch Settling Tests
Characterization of Aggregates
Modeling
Aggregation Kernel
Breakage Kernel
Shear Rate
Solution
Input Parameters and Distribution
Flocculation Kinetics and Modeling
Optimized Parameters
Optimum
Collision frequencies are shown in Figure
Collision
Conclusions

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