Process for preparing magnesium hydroxide whiskers and calcium sulfate from phosphorus tailings
A technology of magnesium hydroxide and phosphorus tailings, which is applied in the field of waste resource utilization and functional nanomaterials, can solve the problems of phosphorus tailings accumulation and environmental pollution, and achieve the effect of high utilization rate and low production cost
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Embodiment 1
[0045] Put 60 kg of phosphorus tailings obtained from flotation into the acid hydrolysis reactor, add 4.415 liters of water, and after reaching the preset temperature of 70°C, slowly add 114.087 liters of 38% hydrochloric acid under stirring conditions, react for 3.5 hours, filter and wash Carry out solid-liquid separation; add 0.323 liters of 30% hydrogen peroxide to the filtrate obtained in the previous step, add ammonia water dropwise under stirring conditions, control the pH value of the filtrate to 6.7, react for 1 hour, filter, and obtain a mixed solution containing magnesium chloride and calcium chloride, labeled It is solution A; put 66.228 kilograms of phosphorus tailings obtained by flotation into another acid hydrolysis reactor, add 247.623 liters of water, after reaching the preset temperature of 50 ° C, slowly add 38.814 liters of 98wt% sulfuric acid under stirring conditions, and react 2 After one hour, filter and wash for solid-liquid separation; add 0.356 liters...
Embodiment 2
[0048] Put 60 kg of phosphorus tailings obtained by flotation into the acidolysis reactor, add 4.415 liters of water, and after reaching the preset temperature of 50°C, slowly add 114.087 liters of 38wt% hydrochloric acid under stirring conditions for reaction, and react for 3.5 hours, filter, Wash for solid-liquid separation; add 0.323 liters of 30wt% hydrogen peroxide to the filtrate obtained in the previous step, and add ammonia water dropwise under stirring conditions, control the pH value of the filtrate to 6.7, react for 1 hour, and filter to obtain a mixture containing magnesium chloride and calcium chloride. Solution, marked as solution A; put 66.228 kilograms of phosphorus tailings obtained by flotation into another acid hydrolysis reactor, add 247.623 liters of water, after reaching the preset temperature of 50 ° C, slowly add 38.814 liters of 98wt% sulfuric acid under stirring conditions, After reacting for 2 hours, filter and wash to carry out solid-liquid separatio...
Embodiment 3
[0051] Put 65.5 kg of phosphorus tailings obtained from flotation into the acid hydrolysis reactor, add 4.820 liters of water, and after reaching the preset temperature of 30°C, slowly add 124.545 liters of 38wt% hydrochloric acid under stirring conditions, react for 3.5 hours, filter and wash Carry out solid-liquid separation; add 0.353 liters of 30wt% hydrogen peroxide to the filtrate obtained in the previous step, add ammonia water dropwise to control the pH value of the filtrate to 6.7, react for 1 hour, and filter to obtain a mixed solution containing magnesium chloride and calcium chloride, which is marked as solution A; Put 72.300 kg of phosphorus tailings obtained from flotation into another acid hydrolysis reactor, add 270.322 liters of water, and after reaching the preset temperature of 50°C, slowly add 42.372 liters of 50wt% sulfuric acid under stirring conditions, react for 2 hours, filter, Wash for solid-liquid separation; add 0.389 liters of 30wt% hydrogen peroxid...
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