Liquid phase leaching method of chromite or chromium-iron calcined molten salt
A molten salt and liquid phase technology, applied in the direction of chromate/dichromate, etc., can solve the problems of difficult industrialization, high production cost, furnace charge wall and low conversion rate of chrome ore, etc., to solve the problem of site occupation area Large, avoiding the sudden cooling and explosion of the furnace charge, and reducing the effect of leaching time
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Embodiment 1
[0032]It is used for liquid phase continuous leaching of chromite molten salt. The liquid phase clinker enters through the high-level liquid phase feed port, and after being granulated and cooled by the horizontal rotary wheel, it is leached with water for 10 minutes, filtered, Sodium chromate alkaline solution and iron slag are obtained, and the gas generated during leaching is removed from the flue gas outlet of the gas collecting hood. The conversion and leaching rate of chrome ore (that is, the percentage of chromium in chromite ore converted into soluble chromium in sodium chromate alkaline solution) was determined to be 97.25%, and the iron mass content of iron slag calculated as ferric oxide was 62.31% .
Embodiment 2
[0034] It is used for liquid phase continuous leaching of chromite molten salt. The liquid phase clinker enters through the high-level liquid phase feed port, and after being granulated and cooled by the horizontal rotary wheel, it is leached with water for 15 minutes and filtered. Sodium chromate alkaline solution and iron slag are obtained. The gas produced in the leaching is removed from the flue gas outlet of the gas collection hood. It has been determined that the conversion and leaching rate of chromium ore is 98.19%, and the iron mass content of iron slag calculated as ferric oxide is 58.29%.
Embodiment 3
[0036] It is used for the liquid phase continuous leaching of yellow phosphorite molten salt. The liquid phase clinker enters through the high-level liquid phase feed port, and after being granulated and cooled by the horizontal rotary wheel, it is leached with water and filtered to obtain phosphorus liquid and phosphorus scum. The method of the present invention can also be used for the leaching of yellow phosphorite molten salt.
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