Method for extracting titanium from red mud
A technology of red mud and titanic acid, applied in the field of red mud hydrometallurgy, can solve the problems of low purity of product titanium dioxide, difficult treatment of acidic wastewater, large amount of sodium hydroxide, etc., and achieves less impurities in hydrolyzed products, accelerated destruction, and reduced sulfuric acid. The effect of consumption
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Embodiment 1
[0024] The water leaching slag is discharged into the acid leaching tank, and the mixed solution of sulfuric acid solution and citric acid is added according to the liquid-solid mass ratio of 4 ~ 8mL / g to carry out secondary acid leaching; the mixed solution of the sulfuric acid solution and citric acid is obtained by 3~4mol / L sulfuric acid solution and citric acid with a mass fraction of 6~8% are mixed; then stirred for 60~120min under the condition of stirring intensity of 250~400r / min and leaching temperature of 70~100℃, solid-liquid Separation to obtain tailings and acid leaching solution, acid leaching solution mixed with new red mud water leaching residue for secondary acid leaching, solid-liquid separation to obtain acid leaching residue and qualified titanium-containing acid leaching solution, acid leaching residue is mixed with raffinate, After adding citric acid with a mass fraction of 6-8%, carry out secondary acid leaching, and obtain tailings and qualified titanic ...
Embodiment 2
[0026]The water leaching slag is discharged into the acid leaching tank, and the mixed solution of sulfuric acid solution and citric acid is added according to the liquid-solid mass ratio of 4 ~ 8mL / g to carry out secondary acid leaching; the mixed solution of the sulfuric acid solution and citric acid is obtained by 4~5mol / L sulfuric acid solution and citric acid with a mass fraction of 4~6% are mixed; then stirred for 45~90min under the condition of stirring intensity of 300~500r / min and leaching temperature of 70~100℃, solid-liquid Separation of tailings and acid leaching solution, acid leaching solution mixed with new red mud water leaching residue for secondary acid leaching, solid-liquid separation to obtain acid leaching residue and qualified titanium-containing acid leaching solution, acid leaching residue and raffinate mixed , after adding citric acid with a mass fraction of 4-6%, carry out secondary acid leaching, solid-liquid separation to obtain tailings and qualifi...
Embodiment 3
[0028] The water leaching slag is discharged into the acid leaching tank, and the mixed solution of sulfuric acid solution and citric acid is added according to the liquid-solid mass ratio of 4 ~ 8mL / g to carry out secondary acid leaching; the mixed solution of the sulfuric acid solution and citric acid is obtained by 5~6mol / L sulfuric acid solution and citric acid with a mass fraction of 2~4% are mixed; then stirred for 30~60min under the condition of stirring intensity of 400~600r / min and leaching temperature of 70~100℃, solid-liquid Separation of tailings and acid leaching solution, acid leaching solution mixed with new red mud water leaching residue for secondary acid leaching, solid-liquid separation to obtain acid leaching residue and qualified titanium-containing acid leaching solution, acid leaching residue and raffinate mixed , after adding citric acid with a mass fraction of 2-4%, carry out secondary acid leaching, solid-liquid separation to obtain tailings and qualif...
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