Method for clean production of titanium dioxide by using potassium hydroxide
A technology of potassium hydroxide and titanium dioxide, which is applied in the direction of titanium dioxide, titanium oxide/hydroxide, and fibrous fillers, can solve the problems of low discharge of "three wastes", good product quality, and short process flow, and achieve technical difficulty and The effect of reducing equipment investment costs, reducing production energy consumption, and reducing reaction temperature
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Embodiment 1
[0027] The KOH solution that is circulated back to the reactor and the high titanium slag (TiO 2 The mass content is 87.0%) and mix evenly under stirring, react at 450 ℃ for 0.5 hour, wherein, the mass ratio of high-titanium slag and solid KOH is 1.5:1, obtain solid intermediate product after reaction, at this moment, high-titanium slag decomposition rate is 100%. The intermediate product was washed twice with water at a washing temperature of 55°C, and the solid-to-liquid mass ratio of each wash was 1:10. The filtered product was added to a sulfuric acid solution to adjust the pH value of the system to 0.10. The product was completely dissolved at 45°C, and then iron was added. The powder is used as a reducing agent to convert all ferric iron into ferrous iron. Finally, the obtained titanium solution was filtered, and the filtrate was hydrolyzed at 80°C for 8 hours, and the hydrolyzed product was filtered to obtain a white hydrated titanium dioxide solid, which was calcined ...
Embodiment 2
[0029] The KOH solution that is circulated back to the reactor and the high titanium slag (TiO 2 The mass content is 87.0%) were mixed evenly under stirring, and reacted at 380° C. for 2 hours, wherein the mass ratio of high titanium slag to KOH solid was 0.6:1, and a solid intermediate product was obtained after the reaction, and the decomposition rate of high titanium slag was 98%. The intermediate product is washed with water at normal temperature, the washing solid-liquid mass ratio is 1:100, hydrochloric acid solution is added to the product obtained after filtration, the pH value of the system is adjusted to 0.15, and the unreacted high-titanium slag is filtered out after fully dissolving at normal temperature, and then Add sodium sulfite to the solution to reduce ferric iron to ferrous iron, then filter the obtained titanium solution, hydrolyze the filtrate at 110°C for 4 hours, and filter the hydrolyzed product to obtain a white hydrated titanium dioxide solid, calcinin...
Embodiment 3
[0031] The KOH solution that is circulated back to the reactor and the high titanium slag (TiO 2The mass content is 89.5%) and mixed evenly under stirring, and reacted at 500° C. for 0.5 hours, wherein the mass ratio of high titanium slag to KOH solid was 1:1, and a solid intermediate product was obtained after the reaction, and the decomposition rate of high titanium slag was 100%. Add water and mix the solid intermediate product evenly, carry out the carbonation reaction of the intermediate product at 50°C, and pass CO into the solution 2 The partial pressure is 2MPa, and the solid-liquid mass ratio of the reaction is 1:100. After reacting for 4 hours, filter the product, add hydrochloric acid solution to dissolve, adjust the pH value of the system to 0.30, and dissolve the product completely at 60°C, and then add iron sheet as a reduction agent. agent to convert ferric iron into ferrous iron, then the solution was hydrolyzed at 40°C for 15 hours, and the hydrolyzed product ...
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