Vanadium-titanium magnetite concentrate recleaning method realized through alkaline leaching, desliming and gravity separation
A vanadium-titanium magnetite concentrate and alkali leaching technology, applied in chemical instruments and methods, wet separation, solid separation, etc., to achieve the effects of improving comprehensive utilization, improving blast furnace utilization coefficient, and reducing emissions
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Embodiment 1
[0033] 1) Alkaline leaching
[0034] The TFe content is 50.1%, TiO 2 content of 14.8%, SiO 2 The content is 3.48%, Al 2 o 3 The vanadium-titanium magnetite concentrate with a content of 4.25% and a S content of 0.69% is placed in a NaOH alkali solution with a mass concentration of 40%, and is subjected to alkali leaching reaction at a temperature of 370° C. for 3 hours, and the reactant is filtered to obtain the filtrate and Alkali leaching filter cake A, NaOH consumption 97kg / t feeds ore, and described filtrate is fed into recovery treatment system, and its chemical reaction formula is:
[0035]
[0036]
[0037]
[0038]
[0039]
[0040] 2) Desliming
[0041] 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.
[0042] 3) re-election
[0043] Add water to the grit B in step 2) to ma...
Embodiment 2
[0045] 1) Alkaline leaching
[0046] The TFe content is 51.6%, TiO 2 content of 13.5%, SiO 2 The content is 3.82%, Al 2 o 3 The vanadium-titanium magnetite concentrate with a content of 5.75% and a S content of 0.75% is placed in 30% N a In OH alkali solution, carry out alkali leaching reaction at 260°C for 2 hours, filter the reactants to obtain filtrate and alkali leaching filter cake A, the NaOH consumption is 76kg / t to feed the ore, and the filtrate is fed to the recovery treatment system , its chemical reaction formula is with embodiment 1.
[0047] 2) Desliming
[0048] 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.
[0049] 3) re-election
[0050] Add water to the grit B in step 2) to make a slurry with a mass concentration of 36% and feed The spiral chute of rice is carried out gravity separat...
Embodiment 3
[0052] 1) Alkaline leaching
[0053] The TFe content is 53.7%, TiO 2 content of 12.2%, SiO 2 The content is 4.15%, Al 2 o 3 The vanadium-titanium magnetite concentrate with a content of 5.37% and a S content of 0.82% is placed in a NaOH alkali solution with a mass concentration of 20%, and is subjected to alkali leaching reaction at a temperature of 340° C. for 5 hours, and the reactant is filtered to obtain a filtrate and Alkali leaching filter cake A, NaOH consumption 84kg / t feeds ore, and described filtrate feeds recovery processing system, and its chemical reaction formula is the same as embodiment 1.
[0054] 2) Desliming
[0055] 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.
[0056] 3) re-election
[0057] Add water to the grit B in step 2) to make a slurry with a mass concentration of 4...
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