Method for re-selecting vanadium-titanium magnetite concentrate by alkali leaching, pickling, desliming and gravity-magnetism
A vanadium-titanium magnetite concentrate and alkali leaching technology, applied in chemical instruments and methods, wet separation, solid separation and other directions, to achieve the effects of low cost, improved blast furnace utilization coefficient, and improved comprehensive utilization rate
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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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