Method for decontaminating potassium sub-molten salt soluble crystal liquid and preparing chromic oxide
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] The potassium-based sub-molten salt solution crystal solution from a chromium salt factory was selected
[0038]
[0039] The alkaline liquid obtained by dissolving the crystal liquid of the potassium-based sub-molten salt is pumped into the liquid storage tank, and the temperature is controlled at 60°C. into CO 2 (high purity CO 2Mix with air (volume fraction 55%), neutralize potassium hydroxide for 0.4h; then add aluminum hydroxide seed crystals, the seed coefficient is 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 4 times in countercurrent at 80°C for 30 minutes. After carbon separation, due to the loss of part of the water-soluble chromium in the filter cake, the K in the filtrate 2 CO 3 Slightly lower (90g / L), K 2 CO 3 : 150g / L; KHCO 3 : 62g / L. The filtrate is pre-carbonized, the press...
Embodiment 2
[0041] Select sodium chromate alkaline solution from a chromium salt factory
[0042]
[0043] The alkaline liquid obtained by dissolving the crystal liquid of the potassium-based sub-molten salt is pumped into the liquid storage tank, and the temperature is controlled at 70°C. into CO 2 (high purity CO 2 Mix with air (volume fraction 36%), neutralize potassium hydroxide for 1.0h; then add aluminum hydroxide seed crystals, the seed coefficient is 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 for 15 minutes. After carbon separation, due to the loss of part of the water-soluble chromium in the filter cake, the K in the filtrate 2 CO 3 Slightly lower (190g / L), K 2 CO 3 : 190g / L; KHCO 3 : 86g / L. The filtrate was pre-carbonized at a pressure of 0.6MPa ...
Embodiment 3
[0045] Select sodium chromate alkaline solution from a chromium salt factory
[0046]
[0047] The alkaline liquid obtained by dissolving the crystal liquid of the potassium-based sub-molten salt is pumped into the liquid storage tank, and the temperature is controlled at 60°C. into CO 2 (high purity CO 2 Mix with air (volume fraction 20%), neutralize potassium hydroxide for 0.5h; then add aluminum hydroxide seed crystals, the seed coefficient is 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 4 times in countercurrent at 80°C for 20 minutes. After carbon separation, due to the loss of part of the water-soluble chromium in the filter cake, the K in the filtrate 2 CO 3 Slightly lower (280g / L), K 2 CO 3 : 80g / L; KHCO 3 : 29g / L. The filtrate was pre-carbonized at a pressure of 0.4 MPa for 1.5 hours. A...
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