A method for extracting iron from high-iron and low-silicon laterite iron ore
A technology of laterite and iron ore, applied in the direction of improving process efficiency, etc., to achieve the effects of reducing emissions, improving blast furnace utilization coefficient, and low alkali consumption
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Embodiment 1
[0023] Such as figure 1 shown.
[0024] The mass content of Fe is 40.1%, SiO 2 The content is 2.98%, Al 2 o 3 The laterite iron ore with a content of 11.96% is placed in a NaOH alkali solution with a mass concentration of 55%, and is subjected to alkali leaching reaction in a closed container at a temperature of 120°C for 6.0 hours, and then the reactant is filtered to obtain an alkali leaching filter cake A and filtrate B, NaOH consumption 14.0 kg / t feed ore, its chemical reaction formula is:
[0025] al 2 o 3 +2NaOH 2NaAlO 2 + H 2 o
[0026] tSiO 2 +2NaOH Na 2 O (SiO 2 ) t ↓ + H 2 o
[0027] Filter cake A is the final iron ore concentrate obtained with a TFe content of 66.8%, in which SiO 2The content is 0.45%, Al 2 o 3 The S content is 0.96%, and the S content is 0.02%; the filtrate B is fed into the recycling system.
Embodiment 2
[0029] The TFe content is 49.8%, SiO 2 The content is 0.22%, Al 2 o 3 The laterite iron ore with a content of 8.10% is placed in a NaOH alkali solution with a mass concentration of 4%, and is subjected to alkali leaching reaction in a closed container at a temperature of 210°C for 0.3 hours, and then the reactant is filtered to obtain an alkali leaching filter cake A and filtrate B, NaOH consumption 10.36kg / t feed ore, its chemical reaction formula is the same as embodiment 1.
[0030] Filter cake A is the final iron ore concentrate obtained with a TFe content of 62.1%, in which SiO 2 The content is 0.08%, Al 2 o 3 The content of S is 0.87%, and the content of S is 0.01%; the filtrate B is fed into the recycling system.
Embodiment 3
[0032] The TFe content is 44.2%, SiO 2 The content is 2.54%, Al 2 o 3 The laterite iron ore with a content of 10.82% is placed in a NaOH alkali solution with a mass concentration of 50%, and the alkali leaching reaction is carried out in a closed container at a temperature of 200°C for 4.0 hours, and then the reactant is filtered to obtain an alkali leaching filter cake A and filtrate B, NaOH consumption 19.89kg / t feed ore, its chemical reaction formula is the same as embodiment 1.
[0033] Filter cake A is the final iron ore concentrate obtained with a TFe content of 67.90%, in which SiO 2 The content is 0.12%, Al 2 o 3 The content is 0.66%, and the S content is 0.01%; the filtrate B is fed into the recycling system.
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