A method for reducing the amount of waste acid in the production of titanium dioxide
A technology of titanium dioxide and acid content, applied in the direction of titanium dioxide, titanium oxide/hydroxide, etc., can solve the problems of waste of acid resources, large solid waste, and high energy consumption.
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Embodiment 1
[0021] Acid hydrolysis conditions: acid to mineral ratio 1.60, initial reaction acid concentration 84%.
[0022] Grind 1000kg of qualified titanium concentrate, 325 mesh sieve residue is less than 30%, add 620kg of 55% sulfuric acid and mix evenly, then add 1280kg of 98% sulfuric acid to initiate the main reaction, the initiation temperature is greater than 150°C, and the solid phase is at 200°C Aging for 30 minutes, adding 3000L water for leaching for 30 minutes, adding iron powder to reduce until the trivalent titanium disappears, and obtaining a qualified acid-liberation material titanium solution A, and testing related indicators, 55% of sulfuric acid is prepared from waste acid and concentrated sulfuric acid.
Embodiment 2
[0024] Acid hydrolysis conditions: acid to mineral ratio 1.60, initial reaction acid concentration 84%.
[0025] Grind 1000kg of qualified titanium concentrate, and the residue on 325 mesh sieve is less than 30%, add 1090kg of 55% sulfuric acid and mix evenly, add 660kg of SO 3 , to initiate the main reaction, the initiation temperature is greater than 150°C, the solid phase is matured at 200°C for 30 minutes, added 3000L water for leaching for 30 minutes, added iron powder to reduce until the trivalent titanium disappears, and the qualified acid-release material titanium liquid B is obtained, and the test is related Indicators, 55% of sulfuric acid is configured from waste acid and concentrated sulfuric acid.
Embodiment 3
[0027] Acid hydrolysis conditions: acid to mineral ratio 1.60, initial reaction acid concentration 75%.
[0028] Grind 1000kg of qualified titanium concentrate, and the residue on 325 mesh sieve is less than 30%, add 1700kg of 55% sulfuric acid and mix evenly, add 370kg of SO 3 , to initiate the main reaction, the initiation temperature is greater than 150°C, the solid phase is matured at 200°C for 30 minutes, added 3000L water for leaching for 30 minutes, added iron powder to reduce until the trivalent titanium disappears, and obtains qualified acid-release material titanium solution C, which is detected Indicators, 55% of sulfuric acid is configured from waste acid and concentrated sulfuric acid.
[0029] Table 1 is the reaction parameter of each embodiment
[0030] serial number
[0031] Experimental data show that: the invented process can not only increase the recycling amount of waste acid, reduce the generation amount of waste acid, but will not affect the qu...
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