Method of metal recovery
A recovery method and metal technology, applied in chemical instruments and methods, improvement of process efficiency, control of water treatment parameters, etc., can solve problems such as washing liquid waste
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Embodiment 1
[0047] The tantalum raw material compound and the reducing agent are put into the diluted salt heated to about 870°C and in a molten state, and the reduction reaction is carried out. Here, the K 2 TaF 7 It is used as a tantalum raw material compound, KF is used as a diluent salt, and Na is used as a reducing agent.
[0048] After the reduction reaction is finished, the molten reaction solution in the molten state is cooled, and the prepared agglomerate is firstly washed with water. The wastewater prepared here is referred to as the first wastewater. Next, washing was performed with 3% hydrofluoric acid. The wastewater prepared here is referred to as the second wastewater. Then wash with 1.5% hydrogen peroxide water and 9% nitric acid. The wastewater prepared here is referred to as the third wastewater.
[0049] The first wastewater was analyzed by ICP. In terms of metal, the first wastewater contained 610 ppm of tantalum and / or tantalum compounds, but the dissolved tanta...
Embodiment 2~3
[0055] About 1st waste water and 2nd waste water, it processed similarly to Example 1.
[0056] On the other hand, in addition to changing the amount of the pH adjustment solution and the oxidation-reduction potential adjustment solution added to the third wastewater, and making the pH and oxidation-reduction potential of the third wastewater the values shown in Table 1, the same as in Example 1 The 3rd waste water was processed similarly.
[0057] Moreover, the 1st waste water, the 2nd waste water, and the 3rd waste water were mixed similarly to Example 1, and this was recovered by membrane processing. As a result, 95% (in terms of metal) of tantalum and / or tantalum compounds contained in the first wastewater, the second wastewater, and the third wastewater could be recovered.
Embodiment 4~13
[0064] About 1st waste water and 2nd waste water, it processed similarly to Example 1.
[0065] On the other hand, instead of adding the pH adjustment solution to the third wastewater, only the oxidation-reduction potential adjustment solution was added, and the amount was appropriately changed so that the pH and oxidation-reduction potential of the third wastewater were the values shown in Tables 2 to 3. The third wastewater was treated in the same manner as in Example 1.
[0066] Moreover, the 1st waste water, the 2nd waste water, and the 3rd waste water were mixed similarly to Example 1, and this was recovered by membrane processing. As a result, 99% (in terms of metal) of tantalum and / or tantalum compounds contained in the first waste water, the second waste water, and the third waste water could be recovered.
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