Method for preparing high-purity TiO2 from titanium concentrates through oxygen-enriched selective leaching
A titanium concentrate and selective technology, applied in the field of oxygen-enriched selective leaching of titanium concentrate to prepare high-purity TiO2, can solve the problems of high equipment requirements, difficult separation of impurities, increased water consumption in the washing process, etc., and achieve the goal of optimizing dynamic conditions Effect
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Embodiment 1
[0040] Crush the titanium concentrate to a particle size of ≤0.125mm, complete the activation treatment, and obtain titanium concentrate powder; place the titanium concentrate powder in an autoclave for alkaline leaching with a sodium hydroxide solution, wherein the mass concentration of the sodium hydroxide solution is 20 %, the ratio of sodium hydroxide solution to vanadium-titanium concentrate powder is 15:1 according to the liquid-solid ratio; first feed oxygen into the autoclave, then heat up to 180 ° C, keep warm for 3 hours under stirring conditions, and complete the alkali leaching; The material after alkali leaching is filtered and separated to obtain alkali decomposition products and alkali leaching solution; the alkali decomposition products are washed with water until the filtrate is neutral to make alkali decomposition slag; the alkali leaching solution uses CaO as a precipitant to remove SiO 2 , when SiO in liquid phase 2 After the mass percentage of ≤0.05%, it c...
Embodiment 2
[0044] Method is with embodiment 1, and difference is:
[0045] (1) The weight concentration of the sodium hydroxide solution is 30%, and the ratio of the sodium hydroxide solution to the vanadium-titanium magnetite powder is 10:1 according to the liquid-solid ratio; the alkali leaching temperature is 220°C, and the time is 2h;
[0046] (2) the mass concentration of hydrochloric acid is 18%, and the ratio of hydrochloric acid and alkali decomposition slag is 8:1 by liquid-solid ratio; Crystal seed is titanium dioxide, and add-on is 0.3% of alkali decomposition slag gross weight; 150℃, time 2h;
[0047] (3) Concentrate the hydrochloric acid produced by atomizing and absorbing hydrogen chloride gas to a mass concentration of 18%; wash and dry the acid leaching residue and then calcinate at 850°C for 40min; rutile type high-purity TiO 2 Contains TiO by mass percentage 2 99.17%, SiO 2 0.08%,
[0048] CaO2 o 3 0.02, Mn<0.05%, S<0.05%.
Embodiment 3
[0050] Method is with embodiment 1, and difference is:
[0051] (1) The weight concentration of sodium hydroxide solution is 40%, and the ratio of sodium hydroxide solution and vanadium-titanium magnetite powder is 5:1 by liquid-solid ratio; Alkali leaching temperature is 300 ℃, time 1h;
[0052] (2) the mass concentration of hydrochloric acid is 20%, and the ratio of hydrochloric acid and alkali decomposition slag is 10:1 by liquid-solid ratio; 0.2%; pickling hydrolysis temperature 180 ℃, time 1h;
[0053] (3) Concentrate the hydrochloric acid produced by atomizing and absorbing hydrogen chloride gas to a mass concentration of 20%; wash and dry the acid leaching residue and then calcinate at 800°C for 60 minutes; rutile type high-purity TiO 2 Contains TiO by mass percentage 2 99.52, SiO 2 0.05%, CaO2 o 3 0.01%, Mn<0.05%, S<0.05%.
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