Pretreatment method of extraction agent for cobalt-nickel separation and corresponding extraction method
A technology of pretreatment and extraction agent, applied in the field of extraction agent for nickel separation and cobalt, which can solve the problems of difficult recycling, high COD extraction wastewater, etc.
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Embodiment 1
[0042] Extractant pretreatment is performed by the following steps:
[0043] Using sulfonated kerosene as a diluent, the extractant P507 and Cyanex272 were respectively prepared into multiple groups of organic phases with a concentration of 0.25mol / L;
[0044] Mix multiple groups of sodium acetate aqueous solutions of different concentrations as shown in Table 1 with the organic equal volume ratio of the above-mentioned extractant for 15 minutes, then stand for phase separation, and take the obtained organic phase as the pretreated extractant.
[0045] In above-mentioned process, test sodium acetate aqueous solution before and after being used for the pH value of pretreatment, result is as shown in table 1:
[0046] Table 1 Changes in the pH value of the extractant treated with different concentrations of sodium acetate solution
[0047]
[0048] It can be seen that after the sodium acetate solution is treated with the acidic extractant, due to the H +, the pH value decre...
Embodiment 2
[0052] The pretreated extractant obtained by pretreating 0.25mol / L P507 with 3mol / L sodium acetate solution in Example 1 extracts and separates cobalt and nickel mixed feed liquid, wherein the feed liquid is 2g / L Co 2+ and 2g / L Ni 2+ The dilute sulfuric acid aqueous solution, the extraction conditions are: temperature 25 ℃, relative O / A is 1R1, extraction equilibrium time is 15min, the extraction process is as attached figure 1 As shown, the extraction results are shown in Table 2. In the following table and the following examples, the extraction rate is the same extraction rate obtained by extracting the mixed solution of cobalt and nickel coexisting:
[0053] Table 2 Extraction Results
[0054]
[0055] It can be seen that the raffinate obtained from different feed liquids with an initial pH value in the range of 4.60 to 5.80 has the same pH value, and the extraction effect is similar, indicating that the application of the pretreatment method of the present invention do...
Embodiment 3
[0057] The pretreated extractant obtained by pretreating 0.25mol / L P507 with 2mol / L sodium acetate solution in Example 1 extracts and separates cobalt and nickel mixed feed liquid, wherein the feed liquid is 2g / L Co 2+ and 2g / L Ni 2+ pH = 5.40 dilute sulfuric acid aqueous solution, the extraction conditions and process are the same as in Example 2.
[0058] After extraction, the test shows that the raffinate pH value of this embodiment is 5.01, the extraction rates of cobalt and nickel are 94.62% and 17.34%, respectively, and the separation factor is 83.76.
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