A method for separating vanadium and iron by two-stage selective leaching of stone coal
A selective, stone coal technology, applied in the direction of improving process efficiency, can solve the problems of high vanadium loss, poor adaptability, incomplete separation of vanadium and iron, etc., to achieve high separation efficiency, strong adaptability, and improved purification. The effect of enrichment efficiency
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Embodiment 1
[0020] A method for separating vanadium and iron by two-stage selective leaching of stone coal. The concrete steps of the method described in this embodiment are:
[0021] Step 1. Crush the stone coal until the particle size is less than 15mm, roast it in a non-oxidizing atmosphere at 800-860°C for 60-70 minutes, and then grind it until the particle size is less than 0.074mm, accounting for more than 65%, to obtain the roasted material.
[0022] Step 2, the solid-to-liquid ratio of the roasted material and sulfuric acid solution I is 1: (1.5~2) t / m 3 , acid leaching the roasted material in the sulfuric acid solution I at 20-30°C for 10-20 min to obtain an iron-containing acid leaching solution and a first-stage acid leaching residue.
[0023] The volume concentration of the sulfuric acid solution I is 5-6%.
[0024] Step 3, according to the solid-to-liquid ratio of the roasting material and sulfuric acid solution II is 1: (1.5~2) t / m 3 , acid leaching the first-stage acid l...
Embodiment 2
[0030] A method for separating vanadium and iron by two-stage selective leaching of stone coal. The concrete steps of the method described in this embodiment are:
[0031] Step 1: Crush the stone coal until the particle size is less than 15mm, roast in a non-oxidizing atmosphere at 820-880°C for 65-75 minutes, and then grind until the particle size is less than 0.074mm and account for more than 65% to obtain the roasted material.
[0032] Step 2, the solid-to-liquid ratio of the roasted material and sulfuric acid solution I is 1: (2 ~ 2.5) t / m 3 , acid leaching the roasted material in the sulfuric acid solution I for 15-25 min at 25-35°C to obtain an iron-containing acid leaching solution and a first-stage acid leaching residue.
[0033] The volume concentration of the sulfuric acid solution I is 5.5-6.5%.
[0034] Step 3, according to the solid-to-liquid ratio of the roasting material and sulfuric acid solution II is 1: (2 ~ 2.5) t / m 3 , acid leaching the first-stage acid ...
Embodiment 3
[0040] A method for separating vanadium and iron by two-stage selective leaching of stone coal. The concrete steps of the method described in this embodiment are:
[0041] Step 1. Crush the stone coal until the particle size is less than 15mm, roast it in a non-oxidizing atmosphere at 840-900°C for 70-80 minutes, and then grind it until the particle size is less than 0.074mm, accounting for more than 65%, to obtain the roasted material.
[0042] Step 2, according to the solid-to-liquid ratio of the roasting material and sulfuric acid solution I is 1: (2.5 ~ 3) t / m 3 , acid leaching the roasted material in the sulfuric acid solution I for 20-30 min at 30-40°C to obtain an iron-containing acid leaching solution and a first-stage acid leaching residue.
[0043] The volume concentration of the sulfuric acid solution I is 6-7%.
[0044] Step 3, according to the solid-to-liquid ratio of the roasting material and sulfuric acid solution II is 1: (2.5 ~ 3) t / m 3 , acid leaching the ...
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