A method for removing impurities and preparing chromium oxide in a potassium-based sub-molten salt solution
A sub-molten salt and chromium oxide technology is applied in the field of solution crystal liquid removal and chromium oxide preparation after the reaction of chromium salt production sub-molten salt. problems such as long aging time, to achieve the effect of easy filtration and washing, low chromium band loss, and coarse particles
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Embodiment 1
[0037] Choose potassium sub-molten salt solution from a chromium salt factory
[0038]
[0039] The alkaline solution obtained from the potassium-based sub-molten salt solution crystal solution is pumped into the storage tank, and the temperature is controlled to 60°C. Access to CO 2 (High purity CO 2 Mix with air, volume fraction 55%), neutralize potassium hydroxide for 0.4h; then add aluminum hydroxide seed crystals with a seed crystal coefficient of 0.5, neutralize and remove aluminum. The cumulative decomposition time is 2h. The removal rate of carbon and aluminum is 99.9%, and the removal rate of silicon is 98.5%. The aluminum hydroxide filter cake was washed countercurrently for 4 times, the temperature was 80°C, and the time was 30 minutes. After carbon content, the filter cake loses part of the water-soluble chromium, K in the filtrate 2 CO 3 Slightly reduced (90g / L), K 2 CO 3 :150g / L; KHCO 3 : 62g / L. The filtrate is pre-carbonized, the pressure is 0.8MPa, and the time...
Embodiment 2
[0041] Choose sodium chromate alkaline solution from a chromium salt factory
[0042]
[0043] The alkaline solution obtained from the potassium-based sub-molten salt solution crystal solution is pumped into the storage tank, and the temperature is controlled at 70°C. Access to CO 2 (High purity CO 2 Mix with air, volume fraction 36%), neutralize potassium hydroxide for 1.0h; then add aluminum hydroxide seed crystals with a seed crystal coefficient of 1.0, neutralize and remove aluminum. The cumulative decomposition time is 3h. The removal rate of carbon and aluminum is 99.5%, and the removal rate of silicon is 98.5%. The aluminum hydroxide filter cake was washed 4 times in countercurrent, at a temperature of 90°C, and a time of 15 minutes. After carbon content, the filter cake loses part of the water-soluble chromium, K in the filtrate 2 CO 3 Slightly reduced (190g / L), K 2 CO 3 :190g / L; KHCO 3 : 86g / L. The filtrate is pre-carbonized, the pressure is 0.6MPa, and the time is 1....
Embodiment 3
[0045] Choose sodium chromate alkaline solution from a chromium salt factory
[0046]
[0047] The alkaline solution obtained from the potassium-based sub-molten salt solution crystal solution is pumped into the storage tank, and the temperature is controlled to 60°C. Access to CO 2 (High purity CO 2 Mix with air, volume fraction 20%), neutralize potassium hydroxide for 0.5h; then add aluminum hydroxide seed crystals with a seed crystal coefficient of 0.6, neutralize and remove aluminum. The cumulative decomposition time is 2h. The removal rate of carbon and aluminum is 99.1%, and the removal rate of silicon is 98.0%. The aluminum hydroxide filter cake was washed countercurrently for 4 times, the temperature was 80°C, and the time was 20 minutes. After carbon content, the filter cake loses part of the water-soluble chromium, K in the filtrate 2 CO 3 Slightly reduced (280g / L), K 2 CO 3 :80g / L; KHCO 3 : 29g / L. The filtrate is pre-carbonized, the pressure is 0.4MPa, and the time ...
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