Process for regenerating hydrochloric acid for chloridizing laterite nickel ore by wet method
A laterite nickel ore and chlorination treatment technology, applied in the direction of magnesium chloride, chlorine/hydrogen chloride, magnesium halide, etc., can solve the problems of low equipment production capacity, high cost of hydrochloric acid regeneration, high energy consumption, etc., to improve efficiency, improve equipment production capacity and Comprehensive utilization efficiency of energy and full effect of heat utilization
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Embodiment 1
[0024] According to the mass percentage of coal powder in the roasting material is 1%, the mass percentage of the concentrated solution of the mother liquor after nickel precipitation in the roasting material is 50%; The percentage is 49%, and the total moisture content in the material is 50% for material preparation. The concentrated solution of the mother liquor after nickel precipitation, ferric chloride, magnesium chloride crystals obtained when the leaching solution is concentrated, and coal powder are prepared into a slurry and sprayed into a high-temperature furnace. Baking at 750°C.
[0025] The hot hydrogen chloride gas produced during the high-temperature roasting process is directly absorbed by water to obtain regenerated hydrochloric acid, which is returned for pulp leaching. High-viscosity iron oxide and magnesium oxide slags are cooled, crushed and pulverized as by-products.
Embodiment 2
[0027] According to the mass percentage of coal powder in the roasting material is 30%, the mass percentage of the concentrated solution of the mother liquor after nickel precipitation in the roasting material is 40%; The percentage is 30%, and the total moisture content in the material is 45% for material preparation. The concentrated solution of the mother liquor after nickel precipitation, ferric chloride, magnesium chloride crystals obtained when the leaching solution is concentrated, and coal powder are prepared into a slurry and sprayed into a high-temperature furnace. Baking at 700°C.
[0028] The hot hydrogen chloride gas generated during the high-temperature roasting process is directly passed into the laterite nickel ore leachate to heat and concentrate the leachate. The hydrogen chloride gas precipitated from the leachate is cooled and absorbed to regenerate hydrochloric acid or directly used for pulp leaching. High-viscosity iron oxide and magnesium oxide slags are...
Embodiment 3
[0030] According to the mass percentage of coal powder in the roasting material is 60%, the mass percentage of the concentrated solution of the mother liquor after the nickel precipitation in the roasting material is 30%, the mass percentage of ferric chloride and magnesium chloride crystals obtained when the leaching solution is concentrated in the roasting material The percentage is 10%, and the total moisture content in the material is 30% for material preparation. The concentrated solution of the mother liquor after nickel precipitation and the ferric chloride and magnesium chloride crystals obtained when the leaching solution is concentrated are prepared together to form a slurry, and the coal powder is sprayed into high temperature Baked in a furnace at 600°C.
[0031] The hot hydrogen chloride gas generated during the high-temperature roasting process is directly returned to the leaching process for pulp leaching. High-viscosity iron oxide and magnesium oxide slags are ...
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