Neutralization process for wet-process zinc smelting high-acid-leaching low-pollution vanadium precipitation process
A technology of high acid leaching and hydrometallurgy zinc, which is applied in the direction of improving process efficiency, can solve the problems of reducing recovery rate, existing hidden dangers of environmental pollution, loss of zinc and cadmium, etc., and achieves the effect of good process effect.
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Embodiment 1
[0025] Embodiment 1: as figure 1 As shown, a zinc hydrometallurgy high-acid leaching low-pollution sinking alum neutralization process includes four process steps: neutral leaching, low-temperature pre-neutralization, high-temperature high-acid leaching and low-pollution sinking alum for iron removal. In the alum iron removal step, add low-temperature pre-neutralized overflow liquid, ammonium bicarbonate, sodium bicarbonate and cadmium smelting slag, wherein the ratio of parts by weight of ammonium bicarbonate, sodium bicarbonate and cadmium smelting slag is: bicarbonate 1 part of ammonium, 1 part of sodium bicarbonate, 3 parts of cadmium smelting slag; the solid-liquid ratio is 1:10, the pH value of the initial acid is 1.5-1.8, and the pH value of the final acid is 1.6-2.0; the end-point Fe≤3g / L, the reaction temperature is 90 Above ℃, the reaction time is 3 hours; let the ferric ions in the solution become jarosite crystals that are not soluble in sulfuric acid, but also sol...
Embodiment 2
[0026] Embodiment 2: as figure 1 As shown, a zinc hydrometallurgy high-acid leaching low-pollution sinking alum neutralization process includes four process steps: neutral leaching, low-temperature pre-neutralization, high-temperature high-acid leaching and low-pollution sinking alum for iron removal. In the alum iron removal step, add low-temperature pre-neutralized overflow liquid, ammonium bicarbonate, sodium bicarbonate and cadmium smelting slag, wherein the ratio of parts by weight of ammonium bicarbonate, sodium bicarbonate and cadmium smelting slag is: bicarbonate 1 part of ammonium, 2 parts of sodium bicarbonate, 4 parts of cadmium smelting slag; the solid-liquid ratio is 1:8, the pH value of the initial acid is 1.8-2, and the pH value of the final acid is 1.9-2.5; the end point contains Fe≤3g / L, and the reaction temperature is 90 Above ℃, the reaction time is 4 hours; let the ferric ions in the solution become jarosite crystals that are not soluble in sulfuric acid, b...
Embodiment 3
[0027] Embodiment 3: as figure 1 As shown, a zinc hydrometallurgy high-acid leaching low-pollution sinking alum neutralization process includes four process steps: neutral leaching, low-temperature pre-neutralization, high-temperature high-acid leaching and low-pollution sinking alum for iron removal. In the alum iron removal step, add low-temperature pre-neutralized overflow liquid, ammonium bicarbonate, sodium bicarbonate and cadmium smelting slag, wherein the ratio of parts by weight of ammonium bicarbonate, sodium bicarbonate and cadmium smelting slag is: bicarbonate 2 parts of ammonium, 1 part of sodium bicarbonate, 8 parts of cadmium smelting slag; solid-liquid ratio 1:12, initial acid pH value 1.6-1.9, final acid pH value 1.7-2.2; end-point Fe≤3g / L, reaction temperature 90 Above ℃, the reaction time is 5 hours; let the ferric ions in the solution become jarosite crystals that are not soluble in sulfuric acid, but also soluble in precipitation, washing and filtration, an...
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