Method for purifying and enriching vanadium from vanadium-containing solution
A solution and enrichment technology, applied in the field of vanadium-containing shale extraction, can solve the problems of high impurity content and loss of vanadium-containing desorption liquid, and achieve the effects of avoiding loss, low impurity iron concentration and simple process
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Embodiment 1
[0030] A method for purifying and enriching vanadium from a solution containing vanadium. The concrete steps of the method described in this embodiment are:
[0031] Step 1. Preparation of adsorption stock solution
[0032] Adjust the pH value of the vanadium-containing solution to 1.4-2.0, separate the solid and liquid to obtain the clear liquid and neutralized slag; then add an oxidant to the clear liquid until all V(III) and V(IV) in the clear liquid are oxidized into V(V) to obtain the original adsorption solution.
[0033] Step two, resin adsorption
[0034] The adsorption stock solution flows through the D418 aminophosphoric acid chelating resin installed in the ion exchange column at a flow rate of 1-2.5BV / h, and is adsorbed for 30-50 hours to obtain a loaded resin and an adsorption lower solution.
[0035] The height:diameter ratio of the ion exchange column is (5-13):1.
[0036] Step 3. Loaded resin desorption
[0037] Flow pure water through the loaded resin in ...
Embodiment 2
[0045] A method for purifying and enriching vanadium from a solution containing vanadium. The concrete steps of the method described in this embodiment are:
[0046] Step 1. Preparation of adsorption stock solution
[0047] Adjust the pH value of the vanadium-containing solution to 1.8-2.4, separate the solid and liquid to obtain the clear liquid and neutralized slag; then add an oxidant to the clear liquid until all V(III) and V(IV) in the clear liquid are oxidized into V(V) to obtain the original adsorption solution.
[0048] Step two, resin adsorption
[0049] The adsorption stock solution flows through the D418 aminophosphoric acid chelating resin installed in the ion exchange column at a flow rate of 2-4BV / h, and is adsorbed for 20-35 hours to obtain a loaded resin and an adsorption lower solution.
[0050] The height:diameter ratio of the ion exchange column is (10-18):1.
[0051] Step 3. Loaded resin desorption
[0052] Flow pure water through the loaded resin in t...
Embodiment 3
[0060] A method for purifying and enriching vanadium from a solution containing vanadium. The concrete steps of the method described in this embodiment are:
[0061] Step 1. Preparation of adsorption stock solution
[0062] Adjust the pH value of the vanadium-containing solution to 2.2 to 2.6, separate the solid and liquid to obtain the clear liquid and neutralized slag; then add an oxidant to the clear liquid until all V(III) and V(IV) in the clear liquid are oxidized into V(V) to obtain the original adsorption solution.
[0063] Step two, resin adsorption
[0064] The adsorption stock solution flows through the D418 aminophosphoric acid chelating resin installed in the ion exchange column at a flow rate of 3.5-5BV / h, and is adsorbed for 8-20 hours to obtain a loaded resin and an adsorption lower solution.
[0065] The height:diameter ratio of the ion exchange column is (15-25):1.
[0066] Step 3. Loaded resin desorption
[0067] Flow pure water through the loaded resin ...
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