Crystal form regulation and control method for producing titanium dioxide through chlorination process
A titanium dioxide and crystal form control technology, applied in the direction of titanium dioxide, titanium oxide/hydroxide, etc., can solve the problems of short reaction time, affecting product application performance, and not being able to meet the use of high-grade rutile titanium dioxide, achieving low cost and simple operation Effect
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Embodiment 1
[0019] Under the pressure of 200kPa, the chlorine gas at 60°C and the titanium tetrachloride gas at 450°C are uniformly mixed and then introduced into the aluminum trichloride generator; the quantitative aluminum powder in the aluminum trichloride generator and the chlorine gas in the mixed gas After reacting to generate aluminum trichloride gas, it is led to the oxidation reactor together with titanium tetrachloride gas; wherein, the mass ratio of chlorine gas and titanium tetrachloride gas is 2‰, and the molar ratio of chlorine gas and aluminum powder is 5:1. Titanium tetrachloride gas mixed with aluminum trichloride and oxygen preheated to 1600℃-1800℃ undergo gas-phase oxidation reaction. After cooling and gas-solid separation, titanium dioxide with rutile content of 93% is obtained.
Embodiment 2
[0021] Under the pressure of 500kPa, the chlorine gas at 80°C and the titanium tetrachloride gas at 480°C are uniformly mixed and then introduced into the aluminum trichloride generator; the quantitative aluminum powder in the aluminum trichloride generator and the chlorine gas in the mixed gas After reacting to generate aluminum trichloride gas, it is led to the oxidation reactor together with titanium tetrachloride gas; wherein, the mass ratio of chlorine gas to titanium tetrachloride gas is 6‰, and the molar ratio of chlorine gas to aluminum powder is 2:1. Titanium tetrachloride gas mixed with aluminum trichloride and oxygen preheated to 1600℃-1800℃ undergo gas-phase oxidation reaction. After cooling and gas-solid separation, titanium dioxide with a rutile content of 97.8% is obtained.
Embodiment 3
[0023] Under the pressure of 400kPa, the chlorine gas at 70°C and the titanium tetrachloride gas at 410°C are uniformly mixed and then introduced into the aluminum trichloride generator; the quantitative aluminum powder in the aluminum trichloride generator and the chlorine gas in the mixed gas After reacting to generate aluminum trichloride gas, it is led to the oxidation reactor together with titanium tetrachloride gas; wherein, the mass ratio of chlorine gas and titanium tetrachloride gas is 5‰, and the molar ratio of chlorine gas and aluminum powder is 2:1. Titanium tetrachloride gas mixed with aluminum trichloride and oxygen preheated to 1600℃-1800℃ undergo gas-phase oxidation reaction. After cooling and gas-solid separation, titanium dioxide with rutile content of 98.6% is obtained.
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