Abstract
Mechano-chemical treatment has been recognized to be a promising technology for the immobilization of heavy metals (HMs) in contaminated soils without the use of additional reagents. Despite this, very few studies aiming to investigate the applicability of this technology at full scale have been published so far. In this study, a quantitative approach was developed to provide process design information to scale-up from laboratory- into pilot-scale mechano-chemical reactors for immobilizing heavy metals in contaminated mining soil. In fact, after preliminary experiments with laboratory-scale ball mills, experiments have been carried out by taking advantage of milling devices suited for pilot-scale applications. The experimental data of this work, along with literature ones, have been quantitatively interpreted by means of a mathematical model allowing to describe the effect of milling dynamics on the HM immobilization kinetics for applications at different scales. The results suggest that the mechanical process can trigger specific physico-chemical phenomena leading to a significant reduction of HMs leached from mining soils. Specifically, after suitably prolonged processing time, HM concentration in the leachate is lowered below the corresponding threshold limits. The observed behavior is well captured by the proposed model for different HMs and operating conditions. Therefore, the model might be exploited to infer design parameters for the implementation of this technique at the pilot and full scale. Moreover, it represents a valuable tool for designing and controlling mechano-chemical reactors at productive scale.
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Abbreviations
- C R :
-
Charge ratio (–)
- f :
-
Collision frequency (h−1)
- J min :
-
Minimal number of effective collisions (–)
- k :
-
Kinetic constant (h−1)
- k ′ :
-
Kinetic constant (h−1)
- K :
-
Probability of collision (–)
- n :
-
Number of collisions (–)
- m ∗ :
-
Mass involved in physico-chemical transformations (g)
- m :
-
Total mass available within the milling device (g)
- P j :
-
Probability of occurrence an effective hits after j collisions (–)
- q :
-
Total mass fraction of the generic heavy metal (g g−1)
- V l :
-
Volume of the liquid within the mill (L)
- V S :
-
Volume of the solid within the mill (L)
- α :
-
Constant (–)
- ε :
-
Relative error (–)
- ξ :
-
Mass fraction of the generic metal (g g−1)
- ρ S :
-
Density of the solid (g L−1)
- τ :
-
Generic mechanical processing time (h)
- ψ :
-
Mass fraction of the immobilized metal (g g−1)
- HM :
-
Heavy metal
- 0 :
-
Initial condition
- f :
-
Final concentration after leaching
- j :
-
Number of effective collisions
- l :
-
Liquid
- S :
-
Solid
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Concas, A., Montinaro, S., Pisu, M. et al. Experiments and modeling of mine soil inertization through mechano-chemical processing: from bench to pilot scale using attritor and impact mills. Environ Sci Pollut Res 27, 31394–31407 (2020). https://doi.org/10.1007/s11356-020-09445-1
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DOI: https://doi.org/10.1007/s11356-020-09445-1