Method for extracting nickel, cobalt and iron from limonite
A technology of limonite and ore, applied in the direction of improving process efficiency, etc., can solve the problems of uneconomical and effective development and utilization of iron, expensive installation and maintenance, low leaching rate of nickel and cobalt, etc., to achieve efficient development and utilization, and avoid equipment Expensive, low sulfuric acid consumption effect
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Embodiment 1
[0029] 1. Washing and classifying limonite ore, separating coarser minerals such as gravel and sandstone in limonite from the raw ore to obtain high-silicon-magnesium ore and low-silicon-magnesium ore;
[0030] 2. Set +80 purpose 2 # 500kg of high-silicon magnesium ore plus 500kg of water is prepared to obtain 50wt% ore slurry, which is for use;
[0031] 3. Simultaneously add 450kg of 98% concentrated sulfuric acid heated to 150°C to the double-screw pusher reactor and step 2 to prepare 50wt% ore pulp heated to 60°C. After mixing, it will be pushed out by the double-screw pusher reactor for the entire reaction time After 10 minutes, the material released by the double-screw pusher reactor is a crisp honeycomb solid paste, ready for use;
[0032] 4. Simply crush the crisp honeycomb solid paste obtained in step 3, pour it into a water immersion tank after crushing, add water equal to the weight of the crisp honeycomb solid paste, carry out the water dissolving step, and stir fo...
Embodiment 2
[0044] 1. Washing and classifying limonite ore, separating coarser minerals such as gravel and sandstone in limonite from the raw ore to obtain high-silicon-magnesium ore and low-silicon-magnesium ore;
[0045] 2. Add 500kg of water to 500kg of -80 mesh 5# high-silicon magnesium ore to prepare 60wt% ore slurry for use;
[0046] 3. Simultaneously add 450kg of 98% concentrated sulfuric acid heated to 150°C to the double-screw pusher reactor and step 2 to prepare 50wt% ore pulp heated to 60°C. After mixing, it will be pushed out by the double-screw pusher reactor for the entire reaction time After 10 minutes, the material released by the double-screw pusher reactor is a crisp honeycomb solid paste, ready for use;
[0047] 4. Simply crush the crisp honeycomb solid paste obtained in step 3, pour it into a water immersion tank after crushing, add water equal to the weight of the crisp honeycomb solid paste, carry out the water dissolving step, and stir for 10 minutes;
[0048] 5. P...
Embodiment 3
[0058] Steps one to five of the present embodiment, the atmospheric pressure acid leaching stage is the same as in embodiment 1, and the 3# low-silicon magnesium ore is replaced by 6# low-silicon magnesium ore in the pressurized leaching stage;
[0059] 6. Weigh 30 kg of +80 mesh 6# low-silicon magnesium ore obtained in step 1, add 60 L of washing liquid (E1) to prepare limonite slurry, heat it to 95 ° C, and move it into the circulation tank of the pressurized pipeline reactor, and then Add 30L of normal-pressure acid leaching filtrate (B1) at 95°C to the circulation tank of the pressurized pipeline reactor, so that the pH of the solution is 0.8; after sealing the circulation tank, turn on the booster pump, and at the same time turn on the heat transfer oil of the pressurized pipeline reactor Heating device, control the temperature and heat, when the temperature rises to 225°C, continue to heat at a constant temperature for 60 minutes, then stop heating and cool down; after co...
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