The method of re-selecting vanadium-titanium magnetite concentrate by alkali leaching, desliming and magnetic gravity
A vanadium-titanium-magnetite concentrate and magnetic-gravity combined technology, which is applied in chemical instruments and methods, wet separation, solid separation, etc., to achieve the effects of improving comprehensive utilization, reducing ironmaking costs, and reducing emissions
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Embodiment 1
[0039] Such as figure 1 shown.
[0040] 1) Alkaline leaching
[0041] The TFe content is 50.8%, TiO 2 content of 14.9%, SiO 2 The content is 4.96%, Al 2 o 3 The vanadium-titanium magnetite concentrate with a content of 4.87% and a S content of 0.82% is placed in a NaOH alkali solution with a mass concentration of 15%, and is subjected to alkali leaching reaction at a temperature of 370° C. for 3 hours, and the reactant is filtered to obtain a 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:
[0042]
[0043] 2) Desliming
[0044] Add water to the alkali leaching filter cake A in step 1) to prepare a slurry with a mass concentration of 21%, and feed it into a ∮ 3.0-meter desliming hopper for desliming operation to obtain sand settling B and overflow C.
[0045] 3) Combined magnetic gravity beneficiation
[0046] Add water to the grit ...
Embodiment 2
[0049] Such as figure 1 shown.
[0050] 1) Alkaline leaching
[0051] The TFe content is 51.3%, TiO 2 content of 14.2%, SiO 2 The content is 4.71%, Al 2 o 3 The vanadium-titanium magnetite concentrate with a content of 4.99% and a S content of 0.83% is placed in an 8% NaOH alkali solution, subjected to alkali leaching reaction at a temperature of 280° C. for 4 hours, and the reactant is filtered to obtain a filtrate and Alkali leaching filter cake A, NaOH consumption 75kg / t feeds ore, and described filtrate feeds recovery processing system, and its chemical reaction formula is the same as embodiment 1.
[0052] 2) Desliming
[0053] Add water to the alkali leaching filter cake A in step 1) to make a slurry with a mass concentration of 22%, and feed it into a ∮5.0m desliming hopper for desliming operation to obtain sand settling B and overflow C.
[0054] 3) Combined magnetic gravity beneficiation
[0055] Add water to the grit B in step 2) to make a slurry with a mass...
Embodiment 3
[0058] Such as figure 1 shown.
[0059] 1) Alkaline leaching
[0060] The TFe content is 52.7%, TiO 2 content of 13.1%, SiO 2 The content is 4.71%, Al 2 o 3 The vanadium-titanium magnetite concentrate with a content of 4.81% and a S content of 0.82% is placed in a concentration of 30% N a In OH alkaline solution, carry out alkali leaching reaction at 290°C for 5 hours, filter the reactants to obtain filtrate and alkali leaching filter cake A, the NaOH consumption is 85kg / t to feed the ore, and the filtrate is fed to the recovery treatment system , its chemical reaction formula is with embodiment 1.
[0061] 2) Desliming
[0062] Add water to the alkali leaching filter cake A in step 1) to prepare a slurry with a mass concentration of 23% and feed it into a ∮ 3.0-meter desliming hopper for desliming operation to obtain sand settling B and overflow C;
[0063] 3) Combined magnetic gravity beneficiation
[0064] Add water to the grit B in step 2) to make a slurry with a...
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