A kind of method for preparing artificial rutile
An artificial rutile and leaching technology, applied in the direction of titanium dioxide, titanium oxide/hydroxide, etc., can solve the problems of discontinuous production of artificial rutile, low degree of automation, unstable product quality, etc., and achieve low production cost and stable product quality , the effect of high degree of automation
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Embodiment 1
[0041] After being oxidized at 960°C, the titanium concentrate reduced at 820°C is placed in the leaching bin for use. In the acid preparation tank, use concentrated hydrochloric acid and water to prepare a 22% by weight hydrochloric acid solution for use. Pump the prepared acid into the fluidized leaching circulation tank, and use an acid-resistant pump to pump the leached acid into the fluidized leaching In the reaction tower, at the beginning of the leaching operation, when the leaching acid enters the fluidized leaching reaction tower, the graphite heat exchanger is used for heating, and the steam flow is controlled to heat the leaching acid to 80°C to form a fluidized leaching bed; open the modified titanium Concentrate silo discharge valve, by controlling the opening of the discharge valve under the silo, the modified titanium concentrate feed rate is controlled to be continuously fed at 1.5 tons / hour, and the modified titanium concentrate is directly added to the fluidize...
Embodiment 2
[0052] After being oxidized at 1010°C, the titanium concentrate reduced at 860°C is placed in the leaching bin for use. In the acid mixing tank, use concentrated sulfuric acid and water to prepare a sulfuric acid solution with an acid concentration of 21% by weight for use. Pump the prepared acid into the fluidized leaching circulation tank, and use an acid-resistant pump to pump the leached acid into the fluidized leaching In the reaction tower, at the beginning of the leaching operation, the leaching acid is heated by a graphite heat exchanger during the process of entering the fluidized leaching reaction tower, and the steam flow is controlled to heat the leaching acid to 70°C to form a fluidized leaching bed; open the modified titanium Concentrate silo discharge valve, by controlling the opening of the discharge valve under the silo, the modified titanium concentrate is controlled to feed continuously at 1.5 tons / hour, and the modified titanium concentrate is directly added ...
Embodiment 3
[0055] After being oxidized at 970°C, the titanium concentrate reduced at 830°C is placed in the leaching bin for use. In the acid mixing tank, use concentrated sulfuric acid and water to prepare a sulfuric acid solution with an acid concentration of 43% by weight for use. Pump the prepared acid into the fluidized leaching circulation tank, and use an acid-resistant pump to pump the leached acid into fluidized leaching In the reaction tower, at the beginning of the leaching operation, when the leaching acid enters the fluidized leaching reaction tower, the graphite heat exchanger is used for heating, and the steam flow is controlled to heat the leaching acid to 90°C to form a fluidized leaching bed; open the modified titanium Concentrate silo discharge valve, by controlling the opening of the discharge valve under the silo, the modified titanium concentrate is controlled to feed continuously at 1.5 tons / hour, and the modified titanium concentrate is directly added to the fluidiz...
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