Method for producing synthetic rutile
A technology of artificial rutile and a production method, which is applied in the directions of titanium dioxide, titanium oxide/hydroxide, etc., can solve the problems of the artificial rutile leaching process being finely controlled, the solid of the leaching liquid is large, and the calcination temperature is high, and it is easy to continuously The effect of low production and equipment requirements and low calcination temperature
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Embodiment 1
[0022] 2 kg of Panzhihua titanium concentrate (see Table 1 for chemical composition analysis) was first subjected to strong oxidation, the oxidation temperature was 1050 ° C, the oxidant was air, and the oxidation time was 60 minutes; then reduced under the coke oven gas atmosphere, the reduction time was 45 minutes, the reduction Temperature 800 ℃, obtain the titanium ore concentrate after reduction; Get 800 grams of titanium ore concentrates after reduction, acidolysis leaching is heated with distillation flask, and the hydrochloric acid concentration of leaching is 20%, and the liquid-solid ratio of leaching is 3: 1 (ml : g), the leaching time is 5h, the leaching pressure is normal pressure, and the leaching temperature is 100°C. Stir continuously during the leaching process, the extract is cooled and settled, and then the solid phase is filtered, washed, dried at 100°C, and calcined at 500°C. Obtain artificial rutile products. The chemical composition is shown in Table 1,...
Embodiment 2
[0026] The reduced titanium concentrate obtained in Example 1 was subjected to magnetic separation (magnetic field strength 1900 gauss), and 2.5% of non-magnetic tailings and 97.5% of magnetic concentrate were selected. TiO in concentrate 2 The content is 48.10%, SiO 2 The content is 3.09%. 800 grams of magnetic titanium concentrate is heated and acidolysis leached with a distillation flask, the concentration of leached hydrochloric acid is 22%, the ratio of leached liquid to solid is 2.8:1 (ml:g), the leached time is 4 hours, and the leached pressure is normal pressure, and the leaching temperature was 102°C. Stir continuously during the leaching process, the extract is cooled and settled, and then the solid phase is filtered, washed, dried at 100°C, and calcined at 500°C. Obtain artificial rutile products. The chemical composition is shown in Table 2, and the particle size of the artificial rutile is basically the same as that of the original ore. The process recovery r...
Embodiment 3
[0030] The artificial rutile product of Example 2 was subjected to post-magnetic separation (magnetic field strength 6500 Gauss), and the magnetic tailings accounted for 3.2 wt%, and the non-magnetic artificial rutile product accounted for 96.9 wt%. TiO in tailings 2 19.70%, SiO 2 36.4%, MgO 8.85%, CaO 9.26%; the chemical composition of artificial rutile products after magnetic separation is shown in Table 3. The process recovery rate is 96.2%.
[0031] Table 3 gets artificial rutile product chemical composition (wt%) through magnetic separation
[0032] sample name
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