Vanadium-titanium magnetite concentrate recleaning method realized through alkaline leaching, acid pickling, desliming and combined gravity-magnetic separation
A vanadium-titanium-magnetite concentrate and alkali leaching technology is applied in desliming and combined gravity and magnetic separation of vanadium-titanium-magnetite concentrate, pickling, and alkali leaching to achieve mild reaction conditions, reduce emissions, and reduce ironmaking costs Effect
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Embodiment 1
[0042] Such as figure 1 shown.
[0043] 1) Alkaline leaching
[0044] The TFe content is 51.3%, TiO 2 content of 13.7%, SiO 2 The content is 4.55%, Al 2 o 3 The vanadium-titanium magnetite concentrate with a content of 4.71% and a S content of 0.79% is placed in a NaOH alkali solution with a mass concentration of 15%, and is subjected to alkali leaching reaction at a temperature of 300° C. for 1.5 hours, and the reactant is filtered to obtain a filtrate and Alkali leaching filter cake A, NaOH consumption 72kg / t feeds ore, and described filtrate is fed into recovery treatment system, and its chemical reaction formula is:
[0045]
[0046] 2) pickling
[0047] Add water to the alkali leaching filter cake A in step 1) to make a mass solid-liquid ratio of 1: 1.5 ore pulp, then place the mass concentration of 2% H 2 SO 4 In the solution, pickling at 70°C for 8 minutes, filtering the pickling reactants to obtain the filtrate and acid leaching filter cake B, the filtrate i...
Embodiment 2
[0056] Such as figure 1 shown.
[0057] 1) Alkaline leaching
[0058] The TFe content is 51.1%, TiO 2 content of 14.2%, SiO 2 The content is 3.95%, Al 2 o 3 The vanadium-titanium magnetite concentrate with a content of 4.19% and a S content of 0.58% is placed in a NaOH alkali solution with a mass concentration of 25%, and is subjected to alkali leaching reaction at a temperature of 360° C. for 2.5 hours, and the reactant is filtered to obtain a filtrate and Alkali leaching filter cake A, NaOH consumption 82kg / t feeds ore, and described filtrate feeds recovery processing system, and its chemical reaction formula is the same as embodiment 1.
[0059] 2) pickling
[0060] Add water to the alkali leaching filter cake A in step 1) to make a slurry with a mass solid-to-liquid ratio of 1:2.6, and then place the mass concentration in 3% H 2 SO 4 In the solution, acid wash at 75° C. for 60 minutes, and filter the pickling reactants to obtain the filtrate and acid leaching filte...
Embodiment 3
[0068] Such as figure 1 shown.
[0069] 1) Alkaline leaching
[0070] The TFe content is 52.1%, TiO 2 content of 12.6%, SiO 2 The content is 3.05%, Al 2 o 3 The vanadium-titanium magnetite concentrate with a content of 5.31% and a S content of 0.70% was placed in a NaOH alkali solution with a mass concentration of 32%, and was subjected to alkali leaching reaction at a temperature of 310° C. for 3.5 hours, and the reactant was filtered to obtain the filtrate and Alkali leaching filter cake A, NaOH consumption 85kg / t is fed to ore, and described filtrate is fed into recovery treatment system, and its chemical reaction formula is the same as embodiment 1.
[0071] 2) pickling
[0072] Add water to the alkali leaching filter cake A in step 1) to make a slurry with a mass solid-to-liquid ratio of 1:3.8, and then place it in 5% H 2 SO 4 In the solution, acid wash at 50° C. for 50 minutes, and filter the pickling reactants to obtain the filtrate and acid leaching filter cake...
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