Efficient sulfuric acid method titanium dioxide acidolysis process
A technology of sulfuric acid method and titanium dioxide, which is applied in the direction of titanium dioxide, titanium compounds, chemical instruments and methods, etc., can solve the problems of large influence of leaching conditions, influence of leaching rate, and low production efficiency, so as to save sulfuric acid consumption and improve Acid hydrolysis production capacity, the effect of realizing environmental protection production
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Embodiment 1
[0022] Select 30 tons of titanium concentrate with a particle size of less than 0.075mm and less than 0.0374mm and a particle size ratio of 80wt%; add sulfuric acid for acidolysis with an acid-mineral ratio of 1.55, and obtain an acidolysis solid phase; The solution solid phase (temperature is 85 ℃) leaching, the addition rate of leaching water is 100m³ / h; after adding leaching water, add 3m³ of titanium dioxide waste acid to get F value of 1.85; ultrasonic power is 1000W, time is 90min, and then The leaching slurry is beat to the settlement section, the acid hydrolysis rate is 97.3%, and the acid hydrolysis cycle is calculated.
Embodiment 2
[0024] Select 30 tons of titanium concentrate with a particle size of less than 0.075mm and less than 0.0374mm and a particle size ratio of 85wt%; add sulfuric acid for acidolysis with an acid-mineral ratio of 1.6 to obtain an acidolysis solid phase; The leaching of the solid phase (at a temperature of 90°C), the addition rate of the leaching water is 120m³ / h; after adding the leaching water, add 5m³ of titanium dioxide waste acid to obtain an F value of 1.98; the ultrasonic power is 3000W, and the time is 120min, and then the leaching Take the slurry and beat it to the settlement section, the acid hydrolysis rate is 97.6%, and the acid hydrolysis cycle is calculated.
Embodiment 3
[0026] Select 30 tons of titanium concentrate with a particle size of less than 0.075mm and less than 0.0374mm and a particle size of less than 0.0374mm. The leaching of the solid phase (at a temperature of 85°C), the addition rate of the leaching water is 110m³ / h; after the leaching water is added, 4m³ of titanium dioxide waste acid is added to obtain an F value of 1.90; the ultrasonic power is 2000W, and the time is 110min, and then the The leaching slurry is beaten to the settlement section, the acid hydrolysis rate is 97.1%, and the acid hydrolysis cycle is calculated.
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