Vanadium-titanium magnetite concentrate recleaning method realized through alkaline leaching, classification and combined magnetic-gravity separation
A vanadium-titanium-magnetite concentrate and magnetic-gravity combined technology, applied in chemical instruments and methods, solid separation, wet separation, etc., to achieve the effect of improving the utilization factor of blast furnaces, reducing emissions, and reducing ironmaking costs
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Embodiment 1
[0037] Such as figure 1 shown.
[0038] 1) Alkaline leaching
[0039] The TFe content is 52.8%, TiO 2 content of 12.5%, SiO 2 The content is 4.75%, Al 2 o 3 The vanadium-titanium magnetite concentrate with a content of 4.90% and a S content of 0.78% was placed in an 8% NaOH alkali solution, subjected to alkali leaching reaction at a temperature of 300°C for 5 hours, and the reactant was filtered to obtain the filtrate and Alkali leaching filter cake A, NaOH consumption 81kg / t is fed to ore, and described filtrate is fed into recovery treatment system, and its chemical reaction formula is:
[0040]
[0041]
[0042]
[0043]
[0044]
[0045] 2) Grading
[0046] Add water to the alkali leaching filter cake A in step 1) to form an ore slurry with a mass concentration of 20% and feed it into a cyclone for classification, and classify the grit B and overflow Y.
[0047] 3) Combined magnetic gravity beneficiation
[0048] Adding water to the sand settling B i...
Embodiment 2
[0051] Such as figure 1 shown.
[0052] 1) Alkaline leaching
[0053] The TFe content is 51.2%, TiO 2 content of 11.1%, SiO 2 The content is 4.75%, Al 2 o 3 The vanadium-titanium magnetite concentrate with a content of 4.82% and a S content of 0.81% is placed in a NaOH alkali solution with a mass concentration of 15%, and is subjected to alkali leaching reaction at a temperature of 290° C. for 4 hours, and the reactant is filtered to obtain the filtrate and Alkali leaching filter cake A, NaOH consumption 81kg / t feeds ore, and described filtrate feeds recovery processing system, and its chemical reaction formula is the same as embodiment 1.
[0054] 2) Grading
[0055] Add water to the alkali leaching filter cake A in step 1) to form an ore slurry with a mass concentration of 21% and feed it into a cyclone for classification, and classify the grit B and overflow Y.
[0056] 3) Combined magnetic gravity beneficiation
[0057] Add water to the grit B in step 2) to make a ...
Embodiment 3
[0060] Such as figure 1 shown.
[0061] 1) Alkaline leaching
[0062] The TFe content is 50.8%, TiO 2 content of 14.5%, SiO 2 The content is 4.65%, Al 2 o 3 The vanadium-titanium magnetite concentrate with a content of 4.72% and a S content of 0.66% is placed in a NaOH alkali solution with a mass concentration of 22%, and is subjected to alkali leaching reaction at a temperature of 310° C. for 3 hours, and the reactant is filtered to obtain a filtrate and Alkali leaching filter cake A, NaOH consumption 80kg / 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.
[0063] 2) Grading
[0064] Add water to the alkali leaching filter cake A in step 1) to form an ore slurry with a mass concentration of 22% and feed it into a cyclone for classification, and classify the grit B and overflow Y.
[0065] 3) Combined magnetic gravity beneficiation
[0066] Add water to the grit B in step 2) to ...
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