Method for removing iron from leachate of nickel oxide ores
A nickel oxide ore and leaching solution technology, which is applied in the direction of improving process efficiency, can solve problems such as difficulties, loss of ore pulp filtration, and loss of metal ions such as nickel and cobalt in filtration, so as to reduce production costs, simplify the process flow, and have good filtration performance. Effect
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Embodiment 1
[0022] The concentration of metal ions in the nickel oxide ore leaching solution (hereinafter referred to as the leaching solution) is respectively: Fe 2+ 2.02g / L, Fe 3+ 8.5g / L, Ni 2+ 1.2g / L, Co 2+ 0.13g / L, Mg 2+ 0.17g / L, Al 3+ 0.08g / L. The acid concentration of the leaching solution is 12g / L.
[0023] Iron removal method:
[0024] (1) 600ml of water is added to a stirred reactor with a volume of 4L;
[0025] (2) Heat up to 85°C, add the above-mentioned leachate and air into the reaction kettle at a rate of 0.02L / min and 0.01L / min respectively under stirring conditions, and the feeding time of the leachate and air is 2.5h (generally In this case, the feeding of leachate and air is started and stopped at the same time);
[0026] (3) Stop feeding leachate and air, continue to stir and react for 45min, the ore pulp is discharged from the reactor, obtain filtrate and filter residue two parts after filtration, the gained filter residue can be sold as product after drying (g...
Embodiment 2
[0030] The concentrations of metal ions in the leaching solution are: Fe 2+ 1.02g / L, Fe 3+ 2.62g / L, Ni 2+ 1.33g / L, Co 2+ 0.093g / L, Mg 2+ 3.17g / L, Al 3+ 0.6g / L. The acid concentration of the leaching solution was 13g / L.
[0031] Iron removal method:
[0032] (1) 1.1L of water is added into a stirred reactor with a volume of 2.5L;
[0033] (2) Heat up to 75°C, add the above leachate and oxygen into the reaction kettle at a rate of 0.04L / min and 0.005L / min respectively under stirring conditions, and the feeding time of the leachate and air is 30min;
[0034] (3) Stop adding leachate and oxygen, continue to stir and react for 15 minutes, discharge the ore pulp from the reactor, and obtain filtrate and filter residue after filtration. The obtained filter residue can be sold as a product after drying, and the obtained filtrate is the solution after iron removal.
[0035] In the above method, the slurry is very easy to filter, and no sediment passes through the filter cloth. ...
Embodiment 3
[0038] The concentrations of metal ions in the leaching solution are: Fe 2+ 9.3g / L, Fe 3+ 20.6g / L, Ni 2+ 5.2g / L, Co 2+ 0.53g / L, Mg 2+ 7.7g / L, Al 3+ 3.1g / L. The acid concentration of the leaching solution is 15g / L.
[0039] Iron removal method:
[0040] (1) 1.2L of water is added into a stirred reactor with a volume of 4.5L;
[0041](2) Warm up to 95°C, add the above leachate and air at a speed of 0.03L / min and 0.04L / min respectively under stirring conditions, and the leachate and air in the reaction kettle are introduced for 1.5h;
[0042] (3) Stop adding leachate and air, and then stir for 90 minutes to react, discharge the ore pulp from the reactor, and obtain filtrate and filter residue after filtration. The obtained filter residue can be sold as a product after drying, and the obtained filtrate is the solution after iron removal.
[0043] In the above method, the slurry is very easy to filter, and no sediment passes through the filter cloth. The residual acid conc...
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