Method for preparing calcium sulfate from fluorite mine calcium-containing waste liquid
A calcium sulfate and fluorite ore technology, applied in calcium/strontium/barium sulfate, chemical instruments and methods, calcium/strontium/barium compounds, etc., can solve problems such as high maintenance costs, unfavorable process control, and large pipelines
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Embodiment 1
[0041] Specific steps are as follows:
[0042] S1: The calcium-containing waste liquid of fluorite ore and dilute sulfuric acid are sequentially added to the crystallizer for crystallization and precipitation reaction,
[0043] Ca in fluorite ore calcium-containing waste liquid 2+ The mass percent of Ca is 12.49%, and the mass percent of dilute sulfuric acid is 10%, wherein, Ca 2+ Ions and SO 4 2- The molar ratio of ions is 1:0.7;
[0044] S2: control the calcium sulfate crystallization rate generated in the crystallization precipitation reaction by the following means to obtain calcium sulfate crystal slurry,
[0045] Wherein, at room temperature, the feeding rate of the calcium-containing waste liquid is controlled to be 23.5kg / (m 3 h), the feeding rate of dilute sulfuric acid is 56kg / (m 3 h), the crystallization precipitation reaction time of calcium sulfate is 5h, and the stirring linear velocity of crystallizer is 0.8m / s;
[0046] S3: the calcium sulfate crystal sl...
Embodiment 2
[0051] Specific steps are as follows:
[0052] S1: The obtained CaSO will be expected to be produced 4 5% (mole percent) of seed crystals, fluorite ore calcium-containing waste liquid and dilute sulfuric acid are sequentially added to the stirring tank for crystallization and precipitation reaction. The production method is intermittent production.
[0053] Ca in fluorite ore calcium-containing waste liquid 2+ The mass percent of Ca is 19.81%, and the mass percent of dilute sulfuric acid is 20%, wherein, Ca 2+ Ions and SO 4 2- The molar ratio of ions is 1:1;
[0054] S2: control the calcium sulfate crystallization rate generated in the crystallization precipitation reaction by the following means to obtain calcium sulfate crystal slurry,
[0055] Among them, the crystallization and precipitation reaction time of calcium sulfate is controlled at 45°C for 3 hours, and the stirring line speed of the stirring tank is controlled at 0.8m / s;
[0056] S3: the calcium sulfate cry...
Embodiment 3
[0060] Specific steps are as follows:
[0061] S1: The obtained CaSO will be expected to be produced 4 2% (mole percent) of seed crystals, fluorite ore calcium-containing waste liquid and dilute sulfuric acid are sequentially added to the reactor for crystallization and precipitation reaction. The production method is intermittent production.
[0062] Ca in fluorite ore calcium-containing waste liquid 2+ The mass percent of Ca is 24.85%, and the mass percent of dilute sulfuric acid is 50%, wherein, Ca 2+ Ions and SO 4 2- The molar ratio of ions is 1:0.95;
[0063] S2: control the calcium sulfate crystallization rate generated in the crystallization precipitation reaction by the following means to obtain calcium sulfate crystal slurry,
[0064] Among them, the reaction time of calcium sulfate crystallization and precipitation is controlled at 115°C for 24 hours, and the stirring line speed of the reactor is 0.8-1.0m / s;
[0065] S3: the calcium sulfate crystal slurry obtai...
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