Titanium dioxide solution production method capable of reducing acid consumption
A production method and technology of titanium liquid, applied in the direction of chemical instruments and methods, titanium dioxide, titanium compounds, etc., can solve problems such as failure to meet hydrolysis requirements, lower F value, unqualified titanium liquid, etc., to reduce dosage, reduce pressure, The effect of reducing production costs
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Embodiment 1
[0020] The raw material of titanium ore (titanium dioxide content is 44.5%) is sent to the pre-powder process, crushed, passed through a 320 mesh sieve, and the remaining 7.8% is sieved. Adjust the air volume in the acid hydrolysis tank to 150-200m 3 / h, add 42t of sulfuric acid with a concentration of 93% into the acid hydrolysis tank; after homogenizing for 20min, add 27600kg of titanium ore into the acid hydrolysis tank according to the acid ore ratio of 1.52:1. Adjust the air volume to 600-800m 3 / h, feed 2t / h of steam, after the temperature rises to 60°C, stop the steam. After the temperature at the top of the acidolysis tank rises to the highest point, adjust the air volume to 200m?? / h, and ripen for 90min. Add 4t of waste acid to the acid hydrolysis tank (the waste acid after hydrolyzing and washing the titanium solution in the previous process, the concentration is 22.7%) to adjust the F value to 1.92; then add 69m 3 Water is used for leaching, and then iron powder ...
Embodiment 2
[0022] The raw material of titanium ore (titanium dioxide content is 44.5%) is sent to the pre-powder process, crushed, passed through a 320 mesh sieve, and the remaining 7.8% is sieved. Adjust the air volume in the acid hydrolysis tank to 150-200m 3 / h, add 42t of sulfuric acid with a concentration of 93% into the acid hydrolysis tank; after homogenizing for 20min, add 26900kg of titanium ore into the acid hydrolysis tank according to the acid ore ratio of 1.56:1. Adjust the air volume to 600-800m 3 / h, feed 2t / h of steam, after the temperature rises to 60°C, stop the steam. After the temperature at the top of the acidolysis tank rises to the highest point, adjust the air volume to 200m?? / h, and ripen for 90min. Add 3t of waste acid to the acid hydrolysis tank (the waste acid after hydrolyzing and washing the titanium solution in the previous process, the concentration is 22.4%) to adjust the F value to 1.95; then add 67.2m 3 Water is used for leaching, and then iron powde...
Embodiment 3
[0024] The raw material of titanium ore (titanium dioxide content is 44.5%) is sent to the pre-powder process, crushed, passed through a 320 mesh sieve, and the remaining 7.8% is sieved. Adjust the air volume in the acid hydrolysis tank to 150-200m 3 / h, add 42 tons of sulfuric acid with a concentration of 93% into the acid hydrolysis tank; after homogenizing for 20 minutes, add 27200kg of titanium ore into the acid hydrolysis tank according to the acid ore ratio of 1.54:1. Adjust the air volume to 600-800m?? / h, feed 2t / h of steam, and stop the steam after the temperature rises to 60°C. After the temperature at the top of the acidolysis tank rises to the highest point, adjust the air volume to 200m 3 / h, aging 90min. Add 5t of waste acid to the acid hydrolysis tank (the waste acid after hydrolyzing and washing the titanium liquid in the previous process, the concentration is 23.3%) to adjust the F value to 1.97; then add 68m 3 Water is used for leaching, and then iron powde...
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