Hydrometallurgical method for comprehensively recycling components in lateritic nickel ore as products
A technology of laterite nickel ore and hydrometallurgy, applied in the direction of improving process efficiency, can solve problems such as land occupation, environmental pollution, waste of resources, etc., and achieve the effects of cost saving, cost reduction and product quality improvement.
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Embodiment 1
[0021] 2 kg of laterite nickel ore, ground to more than 100 mesh, the main components and contents of this raw material are shown in Table 1.
[0022] Table 1 Each component and content (%) of laterite nickel ore
[0023] components
Ni
co
MgO
Fe
SiO 2
CaO
Cr 2 o 3
MoO 3
content
1.21
0.009
27.6
9.1
43.4
0.21
0.20
0.019
0.032
[0024] The liquid-solid ratio is 2:1, and the leaching conditions are shown in Table 2. 4dm 3 water for leaching, add concentrated sulfuric acid 1.6kg, NH 4 Cl 0.001kg, the leaching temperature is 35-50°C, and the leaching pressure of the high-pressure pipeline is 30Mpa / cm 2 , after leaching for 6 hours, separate the leaching solution and leaching residue, wash and filter.
[0025] Table 2 Leaching conditions
[0026]
[0027] The leaching results are shown in Table 3. Under the leaching conditions described in Table 2, Ni, Co...
Embodiment 2
[0036] 2 kg of laterite nickel ore, ground to more than 80 meshes, the main components and contents of the raw materials are shown in Table 5.
[0037] Table 5 laterite nickel ore ore composition and content (%)
[0038] Ni
co
MgO
SiO 2
Fe
1.9
0.065
14.3
28.7
16.3
[0039] The liquid-solid ratio is 2:1, and the leaching conditions are shown in Table 6. The 2kg raw material adopts the waste water 4dm of Example 1 3 For leaching, add 2.4kg of concentrated sulfuric acid, NH 4 Cl 0.1kg, the leaching temperature is 40-55°C, and the leaching pressure of the high-pressure pipeline is 35Mpa / cm 2 , after leaching for 6 hours, separate the leaching solution and leaching residue, wash and filter. In the leaching process of this embodiment, the waste water of Embodiment 1 is used for recycling, so the complexing agent NH 4 The amount of Cl can be greatly reduced, and there is no need to add water as the leaching solution. ...
Embodiment 3
[0046] 6 kg of laterite nickel ore, ground to more than 80 meshes, the main components and contents of the raw materials are shown in Table 8.
[0047] Table 8 lateritic nickel ore raw ore composition and content (%)
[0048] Ni
co
SiO 2
Fe
MgO
1.5
0.25
15.2
37.8
6.4
[0049] Liquid-solid ratio is 2: 1, and leaching condition is as table 9, has adopted the waste water 4dm in the embodiment two in this example 3 As a leachate, so no need to add water, in the production process, the complexing agent NH 4 The loss of Cl is very small, so only 0.1kg of NH needs to be added 4 Cl is enough. The leaching results are shown in Table 10.
[0050] Table 9 Leaching Conditions
[0051]
[0052] Table 10 Leaching Results
[0053]
[0054] The leaching solution after filtering and washing is adjusted to pH=2.0±0.2 with raw ore, the nickel concentration in the first leaching solution is 6.6g / L, and the Co is 1.1g / L, whi...
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