Method for extracting tungsten through scheelite decomposing
A technology of scheelite and mass percentage, applied in the field of decomposing scheelite to extract tungsten, to achieve the effect of increasing kinetic rate, reducing emission and reagent cost, and reducing burden
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Embodiment 1
[0024] Scheelite (containing WO 3 51%) into the prepared mixed solution, control the H 2 SO 4 The concentration is 2.0mol / L, H 2 o 2 The concentration is 3.0mol / L, the leaching temperature is 50℃, the leaching time is 3h, the liquid-solid ratio is 8:1, the tungsten leaching rate is 98.2%. After filtering and washing, the filter cake is washed three times with pure water to obtain the leaching residue, which is characterized by XRD Figure and SEM image as figure 1 , as shown in 2.
Embodiment 2
[0026] Scheelite (containing WO 3 57%) into the prepared mixed solution, control the H 2 SO 4 The concentration is 1.5mol / L, H 2 o 2 The concentration is 3.5mol / L, the leaching temperature is 60°C, the leaching time is 3h, the liquid-solid ratio is 8:1, and the tungsten leaching rate is 99.0%. After filtering and washing, the filter cake is washed three times with pure water to obtain the leaching residue. The filtrate is thermally decomposed at 90°C, and the precipitation rate of tungsten is 99.3%. The XRD and SEM images of the obtained tungstic acid are as follows image 3 , as shown in 4. The mother liquor is supplemented with consumed sulfuric acid and hydrogen peroxide to return to leaching.
Embodiment 3
[0028] Scheelite (containing WO 3 62%) into the prepared mixed solution, control the H 2 SO 4 The concentration is 2.5mol / L, H 2 o 2 The concentration is 3.5mol / L, the leaching temperature is 60°C, the leaching time is 3h, the liquid-solid ratio is 8:1, and the tungsten leaching rate is 99.2%. After filtering and washing, the filter cake is washed three times with pure water to obtain the leaching residue. The filtrate was passed through SO at 40°C 2 Gas, the precipitation rate of tungsten is 99.1%. The mother liquor is supplemented with consumed sulfuric acid and hydrogen peroxide to return to leaching.
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