Method for preparing manganese sulfate by manganese oxide ore
A technology of manganese oxide ore and manganese sulfate, applied in the direction of manganese sulfate, etc., can solve problems such as difficulty in realizing industrial production, hindering the smooth progress of the reaction, and having no industrial application value, and achieves low price, improved recovery rate and leaching rate, and short reaction time Effect
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Embodiment 1
[0038] Mix 120g ferromanganese ore (containing 22.47% manganese; 32.7% iron) and 330g ferrous sulfate heptahydrate, add 1.2L water, the temperature is 350°C, the pressure is 1MPa, the stirring speed is adjusted to 200 rpm, and react for 0.5 hours. The manganese leaching rate is up to 95%, and the slag grade TFe≥60%. The obtained manganese sulfate solution can meet the production requirements of electrolytic manganese, manganese dioxide, trimanganese tetraoxide and other products after removal of impurities by conventional methods, and can also be removed by conventional methods. After impurity, it is directly concentrated and crystallized, dried and sold as a product.
Embodiment 2
[0040] Mix 120g of ferromanganese ore (containing 22.47% manganese; 32.7% iron) and 18g of sulfur, add 550mL of water, the temperature is 180°C, the pressure is 20MPa, the stirring speed is adjusted to 200 rpm, and the reaction is carried out for 1.5 hours. The leaching rate is up to 90%, and the slag grade TFe is ≥ 45%. The manganese sulfate solution obtained can meet the production requirements of electrolytic manganese, manganese dioxide, trimanganese tetraoxide and other products after removing impurities by conventional methods, and can also remove impurities by conventional methods Afterwards, it is directly concentrated and crystallized, dried and sold as a product.
Embodiment 3
[0042] Mix 120g pyrolusite (containing 20.47% manganese; 8.7% iron) and 135g ferrous sulfate heptahydrate, add 0.5L water, the temperature is 160°C, the pressure is 0.7MPa, the stirring speed is adjusted to 200 rpm, and react for 3 hours. The manganese leaching rate is up to 72%, and the slag grade TFe is more than 50%. The obtained manganese sulfate solution can meet the production requirements of electrolytic manganese, manganese dioxide, trimanganese tetraoxide and other products after removal of impurities by conventional methods, and can also be removed by conventional methods. After impurity, it is directly concentrated and crystallized, dried and sold as a product.
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