Method for preparing hydrogen fluoride and silicon tetrafluoride by using waste materials containing calcium fluoride
A technology containing calcium fluoride and silicon tetrafluoride, applied in the direction of fluorine/hydrogen fluoride, hydrogen fluoride, fluosilicic acid, etc., can solve the problems of complex post-processing and environmental pollution by calcium fluoride-containing waste, and achieve good social benefits and eliminate The effect of stacking and eliminating environmental damage
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Embodiment 1
[0038] The material used in this embodiment is: calcium fluoride sludge 1667kg (water content 40%) after the treatment of fluorine-containing waste water; ) 2 content is 9%wt, other impurity 7%wt.
[0039] at 8M 3 Add 4000kg of 35% fluosilicic acid to the reaction kettle; start stirring, and add 1667kg of sludge containing calcium fluoride; after 2 hours of normal pressure reaction, pump all the materials into the plate and frame filter press, and return the filtered fluosilicic acid to the reaction kettle kettle; then feed 680kg of cleaning water into the plate and frame filter press to clean the solid material, and the cleaned waste water is mixed with fluosilicic acid in the reaction kettle. The calcium fluorosilicate from the filter press is dried, then sent to a rotary reaction furnace and 833kg of 98% sulfuric acid is added; the reaction temperature is 450°C, and the reaction is carried out for 2 hours.
[0040] Reaction products: calcium sulfate 1135kg, hydrogen fluor...
Embodiment 2
[0042] The material used in this embodiment is: calcium fluoride sludge 1667kg (water content 40%) after the treatment of fluorine-containing waste water; ) 2 content is 9%wt, other impurity 7%wt.
[0043] at 8M 3 Add 4000kg of 35% fluosilicic acid to the reaction kettle; start stirring, and add 1667kg of sludge containing calcium fluoride; after 2 hours of normal pressure reaction, pump all the materials into the plate and frame filter press, and return the filtered fluosilicic acid to the reaction kettle kettle; then feed 680kg of cleaning water into the plate and frame filter press to clean the solid material, and the cleaned waste water is mixed with fluosilicic acid in the reaction kettle. The calcium fluorosilicate obtained by pressure filtration is sent into a rotary reaction furnace and 835 kg of 105% sulfuric acid is added; the heating temperature is 200° C., and the reaction is carried out for 4 hours.
[0044] Reaction products: calcium sulfate 1136kg, hydrogen fl...
Embodiment 3
[0046] The material used in this embodiment is: calcium fluoride sludge 1667kg (water content 40%) after the treatment of fluorine-containing waste water; ) 2 content is 9%wt, other impurity 7%wt.
[0047] at 8M 3 Add 4000kg of 35% fluosilicic acid to the reaction kettle; start stirring, and add 1667kg of sludge containing calcium fluoride; after 2 hours of normal pressure reaction, pump all the materials into the plate and frame filter press, and return the filtered fluosilicic acid to the reaction kettle kettle; then feed 680kg of cleaning water into the plate and frame filter press to clean the solid material, and the cleaned waste water is mixed with fluosilicic acid in the reaction kettle. The calcium fluorosilicate obtained by pressure filtration is sent into a rotary reaction furnace and 825 kg of 98% sulfuric acid is added; the heating temperature is 300° C., and the reaction is carried out for 3 hours.
[0048] Reaction products: calcium sulfate 1131kg, hydrogen flu...
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