Method for enriching chromium from laterite ore
A laterite ore enrichment technology, applied in the field of iron and steel metallurgy, can solve the problems of emphasizing separation and recovery, large energy consumption, and complex intercalation of elements, and achieve large-scale industrial production, high comprehensive utilization of resources, and efficient enrichment and recovery. Effect
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Embodiment 1
[0031] After the laterite ore is crushed to a particle size of 3.0mm, mix 12% sodium sulfate with iron ore, and then press it into a 40mm×40mm×31mm agglomerate. The reduction roasting time at ~980°C is 7 hours. After the roasted product is crushed to a particle size of less than 1.0mm, the ore is ground until the particle size is less than 200 mesh and reaches about 90%. Magnetic separation under a magnetic field strength of 1000Gs, the iron removal rate is 93.88%; After the non-magnetic material is separated and dried by solid-liquid, it is placed in the reactor at a mass-liquid-solid ratio (L / S) of 10, and is mixed with 30% dilute H 2 SO 4 solution, leaching at room temperature, the leaching time is 30min, and the obtained chrome concentrate Cr after solid-liquid separation and drying 2 o 3 The grade is 24.92%, Cr 2 o 3 The recovery rate was 71.75%.
Embodiment 2
[0033] After the laterite ore is crushed to a particle size of 3.0mm, mix soda powder with a mass percentage of 12% and iron ore, and then press it into a 40mm×40mm×31mm agglomerate. The reduction roasting time at 1000°C is 7 hours. After the roasted product is crushed to a particle size of less than 1.0mm, the ore is ground until the particle size is less than 200 mesh and reaches about 90%. The iron removal rate is 97.61% under the magnetic field strength of 1000Gs; After the magnetic material is separated and dried by solid-liquid separation, it is then placed in the reactor at a mass-liquid-solid ratio (L / S) of 10, with 30% dilute H 2 SO 4 solution, leaching at room temperature, the leaching time is 30min, and the obtained chrome concentrate Cr after solid-liquid separation and drying 2 o 3 Grade is 35.59%, Cr 2 o 3 The recovery rate was 56.03%.
Embodiment 3
[0035] After the laterite ore is crushed to a particle size of 3.0mm, mix 12% sodium bicarbonate and 4% soda powder with the iron ore, and then press it into a 40mm×40mm×31mm agglomerate, and dry it at 780-800°C Enter the kiln, reduce and roast at 1000-1050°C for 7 hours, crush the roasted product to a particle size of less than 1.0mm, grind the ore until the particle size is less than 200 mesh and reach about 90%, and magnetically separate under 1000Gs magnetic field strength to remove iron The rate is 93.54%; after the non-magnetic material is separated and dried by solid-liquid separation, it is then placed in the reactor at a mass liquid-solid ratio (L / S) of 10, and is mixed with 30% dilute H 2 SO 4 solution, leaching at room temperature, the leaching time is 30min, and the obtained chrome concentrate Cr after solid-liquid separation and drying 2 o 3 The grade is 27.68%, Cr 2 o 3 The recovery rate was 72.03%.
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