Method for producing industrial grade calcium chloride by taking calcium carbide slurry as raw material
A technology of calcium carbide mud and calcium chloride, applied in the direction of calcium/strontium/barium chloride, calcium/strontium/barium halide, etc., can solve the problem of reducing the value of recycling calcium carbide mud and by-product hydrochloric acid, the difficulty of solid-liquid separation, Problems such as low equipment utilization rate, to achieve the effect of significant environmental protection benefits, short process flow and low consumption quota
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Embodiment 1
[0054] First open the tail gas outlet valve, and under stirring conditions, add 106 liters of by-product hydrochloric acid with a concentration of 25.10% and 47 kg of calcium carbide mud into the reactor and mix them. °C, the pH value is 0.5, and a crude calcium chloride solution is obtained. Then add 3.7 kg of bleaching powder, after 25 minutes of oxidation-reduction reaction, when the reaction is complete, the pH value is 1.5. Finally, 5 kg of NP waste residue was added, heated to 100°C with a jacket after reacting for 20 minutes, and kept at a constant temperature for 40 minutes. The light calcium carbonate in the NP waste residue had been completely decomposed by waste hydrochloric acid, and iron phosphate octahydrate and ammonium magnesium phosphate hexahydrate had precipitated completely. Phase pH is 6.5, stop heating, start discharging. After sedimentation, coarse filtration and fine filtration, refined calcium chloride solution is obtained. The refined calcium chlori...
Embodiment 2
[0056] First open the tail gas outlet valve, and under stirring conditions, add 110 liters of by-product hydrochloric acid with a concentration of 25.8% and 50 kg of calcium carbide mud into the reactor for mixing, and the reaction of neutralizing and decomposing calcium carbide mud at 20 min is fully completed, and the temperature of the slurry rises to 80 °C, the pH value is 1.0, and a crude calcium chloride solution is obtained. Then add 3.9 kg of bleaching powder, after 30 minutes of oxidation-reduction reaction, the temperature of the material is 73°C, and the pH value is 2.0. Finally, 5.5 kg of NP waste residue was added, and after 25 minutes of reaction, it was heated from the outside to 110°C and kept at a constant temperature for 30 minutes. The light calcium carbonate in the NP waste residue had been completely decomposed by waste hydrochloric acid, and iron phosphate octahydrate and ammonium magnesium phosphate hexahydrate had completely precipitated. PH is 6.0, sto...
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