Chromium resource recycling and detoxification processing method for chromium slag
A technology of resource recovery and treatment method, which is applied in the field of detoxification treatment of chromium slag and resource recovery and utilization, and achieves the effect of large processing capacity, quick effect, high social and economic benefits
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Embodiment 1
[0045]1) Put 0.5 tons of chromium slag into a hydrothermal kettle, add water to make the solid-to-liquid ratio (w / w) 1:0.5, stir well, add potassium sulfate, potassium persulfate and sodium carbonate to make potassium sulfate in the system The concentration of potassium persulfate is 2 mol / L, the concentration of potassium persulfate is 1 mol / L, and the concentration of sodium carbonate is 1 mol / L, stir well, close the hydrothermal kettle, set the temperature at 30°C, and keep it warm for 10 h.
[0046] 2) After 10 h, stop heating, cool down to room temperature naturally, and let stand for 24 h.
[0047] 3) After standing still, pour out the supernatant containing hexavalent chromium in the upper layer. The solid residue after hydrothermal treatment is subjected to centrifugal washing and dehydration, and the filter residue is dried to obtain a white or white yellowish solid.
[0048] 4) Add an appropriate amount of CaCl to the separated supernatant and the water for washing ...
Embodiment 2
[0053] Take 1 ton of chromium slag and put it into a hydrothermal kettle, then add water to make the solid-to-liquid ratio (w / w) 1:5, stir well, add potassium sulfate, potassium persulfate and sodium carbonate to make the concentration of potassium sulfate in the system 2 mol / L, the concentration of potassium persulfate is 1 mol / L, the concentration of sodium carbonate is 0.1 mol / L, stir well, turn off the hydrothermal kettle, set the temperature at 250°C, keep it warm for 2 h, stop heating and let stand 0.5 h. Other technological process is identical with embodiment 1.
[0054] The concentration of hexavalent chromium leached from the original chromium residue in this example was 265 mg / L, and the concentration of hexavalent chromium leached from the filter residue after treatment was 1.48 mg / L.
Embodiment 3
[0056] Take 1 ton of chromium slag and put it into a hydrothermal kettle, then add water to make the solid-to-liquid ratio (w / w) 1:10, stir well, add potassium sulfate, potassium persulfate and sodium carbonate to make the concentration of potassium sulfate in the system 0.1 mol / L, the concentration of potassium persulfate is 1 mol / L, the concentration of sodium carbonate is 0.5 mol / L, stir well, close the hydrothermal kettle, set the temperature at 120°C, keep it warm for 6h, stop heating and let stand for 48 h. Other technological process is identical with embodiment 1.
[0057] The concentration of hexavalent chromium leached from the original chromium residue in this embodiment was 257 mg / L, and the concentration of hexavalent chromium leached from the filter residue after treatment was 1.26 mg / L.
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