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Research Article

Kinetics and mechanism of oxidation for nickel-containing pyrrhotite tailings

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  • Received: 12 February 2020Revised: 4 May 2020Accepted: 25 May 2020Available online: 27 May 2020
  • Abstract: X-ray powder diffraction, scanning electron microscopy, energy dispersive spectroscopy, thermogravimetry, differential scanning calorimetry and mass spectrometry have been used to study the products of nickel-containing pyrrhotite tailings oxidation by the oxygen in the air. The kinetic triplets of oxidation, such as activation energy (Ea), pre-exponential factor (A) and reaction model (f(α)) being a function of the conversion degree (α), were adjusted by the regression analysis. In case of a two-stage process representation, the first step proceeds under autocatalysis control and ends at α = 0.42. The kinetic triplet of the first step can be presented as Ea = 262.2 kJ/mol, lgA = 14.53 s-1, f(α) = (1 – α)4.11(1 + 1.51·10–4α). For the second step, the process is controlled by the two-dimensional diffusion of the reactants in the layer of oxidation products. The kinetic triplet of the second step: Еa = 215.0 kJ/mol, lgA = 10.28 s-1, f(α) = (–ln(1 – α))–1. The obtained empirical formulae for the rate of pyrrhotite tailings oxidation reliably describe the macro-mechanism of the process and can be used to design automatization systems for roasting these materials.
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Kinetics and mechanism of oxidation for nickel-containing pyrrhotite tailings

  • Corresponding author:

    Alexander M. Klyushnikov    E-mail: amk8@mail.com

  • Institute of metallurgy of the Ural branch of the Russian Academy of Sciences, Yekaterinburg 620016, Russia

Abstract: Abstract: X-ray powder diffraction, scanning electron microscopy, energy dispersive spectroscopy, thermogravimetry, differential scanning calorimetry and mass spectrometry have been used to study the products of nickel-containing pyrrhotite tailings oxidation by the oxygen in the air. The kinetic triplets of oxidation, such as activation energy (Ea), pre-exponential factor (A) and reaction model (f(α)) being a function of the conversion degree (α), were adjusted by the regression analysis. In case of a two-stage process representation, the first step proceeds under autocatalysis control and ends at α = 0.42. The kinetic triplet of the first step can be presented as Ea = 262.2 kJ/mol, lgA = 14.53 s-1, f(α) = (1 – α)4.11(1 + 1.51·10–4α). For the second step, the process is controlled by the two-dimensional diffusion of the reactants in the layer of oxidation products. The kinetic triplet of the second step: Еa = 215.0 kJ/mol, lgA = 10.28 s-1, f(α) = (–ln(1 – α))–1. The obtained empirical formulae for the rate of pyrrhotite tailings oxidation reliably describe the macro-mechanism of the process and can be used to design automatization systems for roasting these materials.

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