Method for treating primary low-grade high-phosphorus manganese ore by acid blending curing
A high-phosphorus manganese ore, low-grade technology, applied in the direction of process efficiency improvement, etc., can solve the problems of unstable microbial transmission variation, not being practically applied, and failing to achieve good results, etc., to achieve good production sustainability and economical comfort Compatibility, easy industrial production, and low cost
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[0022] Example 1: The chemical composition (mass fraction) of the processed manganese-poor and high-phosphorus pyrolusite is: Mn 13.38%, Fe1.70%, Al 2 O 3 0.62%, CaO39.48%, MgO1.26%, P0.146%.
[0023] The process steps used are:
[0024] 1.1 The low-grade primary high-phosphorus manganese ore is crushed to fine-grained raw ore powder, then concentrated acid is added to it and mixed evenly, and then placed for a certain period of time under normal temperature and pressure to fully mature the low-grade manganese ore;
[0025] 1.2 Adjust the concentration of the matured ore powder slurry, and then use dilute acid as the leaching agent under appropriate temperature and normal pressure to make it fully carry out the leaching reaction, and enrich the manganese in the ore in the leaching residue, while the phosphorus is Phosphoric acid enters the leaching solution, so that iron, calcium, magnesium and other elements enter the leaching solution in the form of water-soluble salts;
[0026] 1.3...
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[0029] Example 2:
[0030] The chemical composition (mass fraction) of the treated low-manganese high-phosphorus high-temperature roasted black manganese ore is: Mn18.84%, Fe4.43%, Al 2 O 3 2.52%, CaO50.32%, MgO2.61%, P0.38%.
[0031] The process steps used are the same as in Example 1.
[0032] After the raw ore is crushed, it is sieved to 95% under a 0.2mm sieve. Take 100g of raw ore powder under the sieve, mix it with 80ml industrial dilute nitric acid (concentration 68%) in a reaction vessel, and place it at room temperature for 1.5 days (36h). After maturation, use dilute nitric acid (pH=1) as the leaching agent to adjust the slurry The material concentration is 100g / L, leaching for 2h at a temperature of 40°C, so that phosphorus enters the leaching solution in the form of phosphoric acid, and iron, calcium, magnesium, aluminum, etc., in the form of nitrate. Then it is separated and washed by filtration to obtain manganese-rich slag.
[0033] It was determined that the manganes...
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[0034] Example 3: The chemical composition (mass fraction) of the treated manganese-poor and high-phosphorus ferromanganese ore is: Mn20.91%, Fe18.46%, Al 2 O 3 6.10%, CaO1.51%, MgO0.54%, P0.39%.
[0035] The process steps used are the same as in Example 1.
[0036] After the raw ore is crushed, it is sieved to 95% under the 0.1mm sieve. Take 500g of raw ore powder under the sieve, mix it with 150ml industrial concentrated sulfuric acid (98% concentration) in the reaction vessel, leave it at room temperature for 1 day (24h), use dilute sulfuric acid (pH=1) as the leaching agent after maturation, adjust the slurry The material concentration is 200g / L, leaching for 3h at 60°C, so that phosphorus enters the leaching solution in the form of phosphoric acid, and iron, calcium, magnesium, aluminum, etc. in the form of sulfate. Then it is separated and washed by filtration to obtain manganese-rich slag.
[0037] It is determined that the manganese-rich slag contains Mn45.35% and P0.094%, ...
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