Method for preparing iron oxide red
A technology of iron red and iron ions, which is applied in the chemical industry, can solve the problems of slow dissolution of harmful components, occupying large land for storage, environmental pollution, etc., to solve the problem of iron slag storage, high iron removal efficiency, and environmental burden effect
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example 1
[0034] Take 1L of nickel laterite acid leaching solution, its iron content is 42g / L (98% of which is ferric iron). Adjust its pH to 2.1 with NaOH, add it to an autoclave, control the temperature at 200°C, oxygen partial pressure 0.2MPa, filter after reaction, wash with 3 times the amount of water slurry, and dry at 100°C.
[0035] After analysis, the iron precipitation rate is 96.6%, the iron oxide red content is >97%, and the Ni precipitation rate is <1.9%.
example 2
[0037] Take 1L of nickel laterite acid leaching solution, its iron content is 42g / L (98% of which is ferric iron). Adjust its pH to 2.3 with NaOH, add it to an autoclave, control the temperature at 210°C, cycle the seed crystal 4 times, oxygen partial pressure 0.2MPa, filter after reaction, wash with 3 times the amount of water slurry, and dry at 100°C.
[0038] After analysis, the iron precipitation rate is 98.0%, the iron oxide red>97%, and the Ni precipitation rate<1.2%.
example 3
[0040] Get 1L of solution before zinc ore iron deposit precipitation, its iron content 20g / L (wherein 98% is ferric iron). Adjust its pH to 2.0 with NaOH, add it to an autoclave, control the temperature at 190°C, cycle the seed crystal 4 times, oxygen partial pressure 0.2MPa, filter after reaction, wash with 3 times the amount of water slurry, and dry at 100°C.
[0041] After analysis, the iron precipitation rate is 95.4%, the iron oxide red>95%, and the Zn precipitation rate<1.4%.
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