Method and system for extracting vanadium from stone coal by compound alkali leaching
A technology of compound alkali and stone coal, applied in the field of vanadium extraction from stone coal, can solve the problems of serious environmental pollution, complicated follow-up treatment, high production cost, etc., and achieve the effect of simple operation process, easy industrialization promotion, and high production cost
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Embodiment 1
[0066] Raw materials: Vanadium-containing stone coal is taken from Anhui area, with a vanadium grade of 0.71%.
[0067] The stone coal is coarsely crushed with a crusher and then ground to a fineness of less than 150 μm by a ball mill. The stone coal is roasted at 850°C for 3.0 hours in a roaster to obtain roasted slag, and the flue gas is collected and purified by a flue gas purifier for future use.
[0068] Grind the stone coal roasting slag with a ball mill, sieve it with a 100-mesh sieve, take the sieve and add it to the leaching tank, and add the compound alkali leaching agent from the compound alkali leaching agent storage tank according to the ratio of liquid to solid (weight ratio) of 2:1. Alkali leaching agent, wherein the concentrations of sodium hydroxide and sodium carbonate in the composite alkali leaching agent are 70g / l and 40g / l respectively, and the alkalinity is 142g / l. Stir the reaction at 95°C in a constant temperature water bath for 2h.
[0069] The mixtu...
Embodiment 2
[0077] Raw materials: Vanadium-containing stone coal is taken from Anhui area, with a vanadium grade of 0.71%.
[0078] The stone coal is roughly crushed by a crusher and then ground to a fineness of less than 150 μm by a ball mill. The stone coal is roasted at 850°C for 2.5 hours in a roaster to obtain roasted slag, and the flue gas is collected by a flue gas purifier for purification.
[0079] Grind the stone coal roasting slag with a ball mill, sieve it with a 100-mesh sieve, take the sieve and add it to the leaching tank, and add the compound alkali leaching agent from the compound alkali leaching agent storage tank according to the ratio of liquid to solid (weight ratio) of 2:1. Alkali leaching agent, wherein the concentrations of sodium hydroxide and sodium bicarbonate in the composite alkali leaching agent are 65g / l and 38g / l respectively, and the alkalinity is 132g / l. The reaction was stirred for 2.0 h under a constant temperature water bath at 90°C.
[0080]The mixtu...
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