Method for recovering scandium and titanium from titanium dioxide waste water
A technology of titanium dioxide wastewater and recovery method, which is applied in the field of scandium and titanium recovery in titanium dioxide wastewater, which can solve the problems of high price and late launch of P507 products, and achieve the effects of small site, easy large-scale production, and reduced production costs
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Embodiment 1
[0027] 2m 3 1000L of titanium dioxide wastewater in the reactor, (acidity 2.5mol H 2 SO 4 , containing scandium 16mg / L, titanium 6g / L, TiO 2 / Sc 2 o 3 =375 / 1), adding 50L of P507 and 4% TBP and the remaining volume of kerosene extractant with a concentration of 20% by volume, for single-stage extraction, stirring for 20 minutes, stirring speed 120r / min, equilibrium time 15 Minutes; static stratification, scandium extraction rate 98%, titanium extraction rate 10%, raffinate through oil trap to centrifuge (oil-water separator) or filter membrane to separate oil, and then treated with oil-absorbing felt, the organic Phase content 100mg / L, discharge.
Embodiment 2
[0029] 500L of loaded organic phase after extraction in Example 1, put into 1.5m 3 In the reaction kettle, first wash 3 times with 3N hydrochloric acid, O / A=1 / 1, then use 2mol / L NaOH lye 800L single-stage back extraction, temperature 70C°, stir for 25 minutes, stirring speed 120r / min; static Layered, the stripping rate of scandium is 98%, and the stripping rate of titanium is 98%. 12mol / L H 2 SO 4 Soluble, acidity 3mol / L H 2 SO 4 , containing scandium 1.35g / L, titanium 48g / L, TiO 2 / Sc 2 o 3 =36 / 1.
Embodiment 3
[0031] With the solution 500L in embodiment 2, put into 2.5 m 3 In the reaction kettle, adjust the acidity to 6M, add 50L of extraction agent of 25% P507 and 6% TBP and the remaining volume of kerosene by volume percentage concentration, carry out the second single-stage extraction, stir for 20 minutes, and the stirring speed 120r / min, equilibration time 20 minutes; static layering, scandium extraction rate 95%, titanium extraction rate 12%, the organic phase is back-extracted again, the conditions are the same as in Example 2, after the back-extracted product is dissolved in sulfuric acid, the pH is controlled to be 2 , Scandium oxalic acid precipitation, scandium oxalate was burned at 800C ° for 5 hours to obtain 98% crude scandium oxide.
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