A kind of method for treating molten salt chlorination waste residue by high temperature phase inversion method
A high-temperature phase inversion and molten salt chlorination technology, which is applied in the direction of titanium tetrachloride, alkali metal chloride, titanium halide, etc., can solve the problems of large amount of waste water, difficult industrial application, complex treatment and utilization process, etc., and achieve production High efficiency, the effect of solving the problem of secondary pollution
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Embodiment 1
[0031] The molten salt chlorination waste slag (NaCl 33.35wt%, CaCl 2 9.24wt%, MgCl 2 15.51wt%) carry out high-temperature ceramic vacuum filtration under heat preservation, obtain unreacted residue and return in the molten salt chlorination furnace. The obtained filtrate is transported to a high-temperature reaction furnace preheated to 800°C, the temperature is raised to 1100°C, and sodium silicate (Na 2 SiO 3 ), the control addition is 30.38wt% of the molten salt chlorination waste slag treatment capacity (being 1.0 times of the total molar weight of calcium chloride and magnesium chloride in the chloride filtrate), the reaction temperature is 1100 ℃, and the reaction time is 90min. The high-temperature reaction product is subjected to high-temperature ceramic vacuum filtration to obtain a filtrate with a NaCl content of 95.8%, which is circulated into a molten salt chlorination furnace; after precipitation and slagging, it can be used as a raw material for building mate...
Embodiment 2
[0033] The molten salt chlorination waste slag (NaCl 33.35wt%, CaCl 2 9.24wt%, MgCl 2 15.51wt%) carry out high-temperature ceramic vacuum filtration under heat preservation, obtain unreacted residue and return in the molten salt chlorination furnace. The obtained filtrate is transported to a high-temperature reaction furnace preheated to 800°C, the temperature is raised to 1000°C, and sodium phosphate (Na 3 PO 4 ), the control addition is 28.59wt% of the molten salt chlorination waste residue treatment capacity (being 0.7 times of the total molar weight of calcium chloride and magnesium chloride in the chloride filtrate), the reaction temperature is 1000°C, and the reaction time is 90min. The high-temperature reaction product is subjected to high-temperature ceramic vacuum filtration to obtain a filtrate with a NaCl content of 95.1%, which is circulated into a molten salt chlorination furnace; after precipitation and slagging, it can be used as a raw material for phosphate ...
Embodiment 3
[0035] The molten salt chlorination waste slag (NaCl 38.52wt%, CaCl 2 9.12wt%, MgCl 2 14.35wt%) is carried out high-temperature ceramics centrifugal separation filtration under heat preservation, obtains the unreacted residue and returns in the molten salt chlorination furnace. The obtained filtrate is transported to a high-temperature reaction furnace preheated to 850°C, the temperature is raised to 1200°C, and sodium silicate (Na 2 SiO3 ), the control addition is 28.74wt% of the molten salt chlorination waste residue treatment capacity (being 1.0 times of the total molar weight of calcium chloride and magnesium chloride in the chloride filtrate), the reaction temperature is 1200 ℃, and the reaction time is 60min. The high-temperature reaction product is subjected to high-temperature ceramic centrifugal filtration to obtain a filtrate with a NaCl content of 96.2%, which is circulated into the molten salt chlorination furnace; after precipitation and slagging, it can be used...
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