Method for recovering scandium in waste acidic water from titanium dioxide production
A recovery method and technology of waste acid water, which is applied in the field of recovery of rare earth element scandium, can solve the problems of ineffective use of dilute sulfuric acid heat, troublesome preparation of lotion, etc., and achieve the effects of avoiding a large amount of decomposition, convenient operation and simplified process
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Embodiment 1
[0020] A method for reclaiming scandium in titanium dioxide production waste acid water, it comprises the following steps:
[0021] (1) Extraction: The concentration of scandium in raw titanium white waste acid is 15.68㎎ / L. In the extraction tank, bis(2-ethylhexyl phosphoric acid) P204-tributyl phosphate TBP-kerosene extractant is used for the waste acid water of titanium white production. 3-stage to 6-stage (3-stage in this example) cascade extraction, calculated by volume, P204 is 6% to 15% (6% in this example), TBP is 4% to 6% (6% in this example) ﹪), the rest is kerosene, the volume ratio of extractant to waste acid is 1:5~30, (1:10 in this example), the mixing time is 10min~30min (10min in this example), and the raffinate contains The scandium is 0.83㎎ / L, and the scandium extraction rate is 90% to 99% (94.7% in this example), and the loaded organic phase containing scandium is obtained;
[0022] (2) Washing: Use 1mol / L-3mol / L (2mol / L in this embodiment) sulfuric acid and...
Embodiment 2
[0030] In step (2), the scandium-containing loaded organic phase obtained in step (1) is washed with 2mol / L sulfuric acid and hydrogen peroxide with a concentration of 27% as detergent, and washed in 15 cascades, and the volume ratio of the loaded organic phase to sulfuric acid is 1:1 / 2, the amount of hydrogen peroxide added is 4% of the volume of sulfuric acid, the organic phase is loaded in the first stage, and sulfuric acid is added in the last stage; in order to avoid the decomposition of hydrogen peroxide in the stirring process, the present invention is between the penultimate stage and the penultimate eighth stage Hydrogen peroxide is added in multiple stages. At the same time, in order to make full use of excess hydrogen peroxide, the present invention adds hydrogen peroxide at intervals between the penultimate stage and the penultimate eighth stage. In this embodiment, hydrogen peroxide is added at the penultimate stage and the penultimate stage. TiO in the primary re...
Embodiment 3
[0034] In step (4), filter the stripping solution obtained in step (3) to obtain scandium-rich alkali cake, heat and dissolve the scandium-rich alkali cake in the reaction kettle with 2mol / L hydrochloric acid, and boil to fully dehydrate titanium, and press filter to obtain chlorine Scandium solution;
[0035] The rest are the same as embodiment 1.
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