Self catalyzed reduction ammonia soaking process of deep sea polymetallic nodule in ammonia-ammonium chloride system
A technology of polymetallic nodules and ammonium chloride, applied in the direction of improving process efficiency, etc., can solve the problems of increased carbon monoxide consumption, high energy consumption of ammonia distillation operation, huge leaching equipment, etc., to improve processing capacity, realize autocatalytic reduction, The effect of reducing carbon monoxide consumption
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Embodiment 1
[0046] Take 10g of rough polymetallic nodules, grind to -0.074mm to account for 81%, add to 120g / l NH 3 , 40g / l Cl - , 2.0g / l Co 2+ , 8.6g / l Ni 2+ , 15.5g / l Cu + In the ammonia-ammonium chloride solution, the liquid-solid weight ratio is 40:1, the leaching temperature is 45°C, and the carbon monoxide flow rate is 2m 3 / t·min, leaching for 2.5h. The leaching rate of cobalt is 89.33%.
Embodiment 2
[0048] Take 10g of rough polymetallic nodules, grind to -0.074mm to account for 70%, add to 160g / l NH 3 , 10g / l Cl - , 2.0g / l Co 2+ , 10.2g / l Ni 2+ , 20g / l Cu + In the ammonia-ammonium chloride solution, the liquid-solid weight ratio is 20:1, the leaching temperature is 50°C, and the carbon monoxide flow rate is 1.5m 3 / t·min, leaching for 4h. The leaching rate of cobalt is 91.42%.
Embodiment 3
[0050] Take 10g of rough polymetallic nodules, grind to -0.074mm to account for 50%, add to 100g / l NH 3 , 30g / l Cl - , 1.9g / l Co 2+ , 11.3g / l Ni 2+ , 8g / l Cu + In the ammonia-ammonium chloride solution, the liquid-solid weight ratio is 5:1, the leaching temperature is 55°C, and the carbon monoxide flow rate is 0.4m 3 / t·min, leaching for 4h. The leaching rate of cobalt is 89.7%.
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