Method for purifying and deferrizing electrolytic manganese leach solution
A technology for purifying and removing iron and leachate, which is applied in the field of iron removal for electrolytic metal manganese compound leachate, can solve the problems of high price, increased difficulty of solution, and high cost of use, so as to reduce the cost of iron removal, ensure the effect of iron removal, and reduce the amount of use Effect
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Embodiment 1
[0028] Utilize the method of the present invention, carry out oxidation and iron removal treatment to compound leaching final solution:
[0029] The concentration of water-soluble manganese in the compound acid leaching final solution used in this embodiment is 36.4g / L (as Mn 2+ meter), the acidity concentration is 1.0g / L (in terms of H + total), the solution used is a total of 20m 3 , the specific implementation steps are as follows:
[0030] (1) When the combined leaching solution of electrolytic metal manganese reaches the end of the leaching reaction, measure the Fe in the leaching solution 2+ Concentration of 1.8g / L, calculated Fe in the filtrate 2+ The total amount is 36kg.
[0031] (2) Using the chemical reaction equation:
[0032] MnO 2 +4H + +2Fe 2+ = 2Fe 3+ + Mn 2+ +2H 2 o
[0033] Calculate the total Fe 2+ fully oxidized to Fe 3+ Required MnO 2 (Taste 22wt%) The theoretical value is 127.11kg, add MnO to the acidic leaching solution according to the th...
Embodiment 2
[0043] Using the method of the present invention, the filtrate (clear liquid) obtained after filtering the combined leaching final liquid is subjected to oxidation and iron removal treatment:
[0044] The concentration of water-soluble manganese in the compound acid leaching final solution used in this embodiment is 37.2g / L (as Mn 2+ meter), the acidity concentration is 1.1g / L (in terms of H + ), the specific implementation steps are as follows:
[0045] (1) When the combined leaching solution of electrolytic manganese metal reaches the end of the leaching reaction, pour the acidic leaching solution into a diaphragm filter press to remove solid impurities, obtain an acidic filtrate (clear liquid), and measure its Fe 2+ The concentration is 2.0g / L, Fe in the filtrate is obtained by calculation 2+ The total amount is 40kg.
[0046] (2) Using the chemical reaction equation:
[0047] MnO 2 +4H + +2Fe 2+ = 2Fe 3+ + Mn 2+ +2H 2 o
[0048] Calculate the total Fe 2+ fully ...
Embodiment 3
[0058] Using the method of the present invention, the filtrate (clear liquid) obtained after filtering the combined leaching final liquid is subjected to oxidation and iron removal treatment:
[0059] The concentration of water-soluble manganese in the compound acid leaching final solution used in this embodiment is 36.2g / L (as Mn 2+ meter), the acidity concentration is 1.4g / L (in terms of H + ), the specific implementation steps are as follows:
[0060] (1) When the combined leaching solution of electrolytic manganese metal reaches the end of the leaching reaction, pour the acidic leaching solution into a diaphragm filter press to remove solid impurities, obtain an acidic filtrate (clear liquid), and measure its Fe 2+ The concentration is 1.5g / L, Fe in the filtrate is obtained by calculation 2+ The total amount is 30kg.
[0061] (2) Using the chemical reaction equation:
[0062] MnO 2 +4H + +2Fe 2+ = 2Fe 3+ + Mn 2+ +2H 2 o
[0063] Calculate the total Fe 2+ fully ...
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