Method for preparing calcium sulfate whisker by-product magnesium hydroxide and magnesium ammonium nitrate by decomposing phosphate tailings by nitric acid
A calcium sulfate whisker and magnesium hydroxide technology, applied in the chemical industry, can solve the problems of high energy consumption, low added value of products, and effective utilization of calcium and magnesium grades, achieving high economic efficiency, simple and feasible production process, The effect of improving stability
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Embodiment 1
[0038] Adding phosphorus tailings and water to the slurry mixing tank is adjusted to a slurry with a solid content of 35%, and then, the phosphorus tailings slurry and the mass fraction of 40% nitric acid are mixed and reacted by pumps to the upper and lower parts of the leaching tank, respectively. , the ratio of nitric acid to the sum of the molar amounts of CaO and MgO in phosphorus tailings is 1.8:1, the reaction temperature is controlled at 50°C, and the reaction time is 1.5h. Filter residue I and mother liquor I are obtained by filtration and separation, and filter residue I is used to make cement; The mother liquor I enters the metathesis tank, and ammonium bisulfate is added to the metathesis tank according to the molar ratio of CaO of 1:1, the reaction temperature is controlled at 85°C, the stirring speed is 250r / min, and the reaction material is cooled to 40°C after 1.0h of reaction. And keep warm for crystallization for 2.0h, then filter and separate, and wash the fi...
Embodiment 2
[0041] Phosphorus tailings and water are added to the slurry mixing tank to prepare a slurry with a solid content of 10%, and then the phosphorus tailings slurry and dilute nitric acid with a mass fraction of 45% are mixed and reacted to the upper and lower parts of the leaching tank through a pump. Among them, the ratio of nitric acid to the sum of the molar amounts of CaO and MgO in phosphorus tailings is 2.0:1, the reaction temperature is controlled at 70°C, the reaction time is 1.0h, and the filter residue I and mother liquor I are obtained by filtration and separation. Fertilizer; according to the molar ratio of CaO 1:1.05, add sulfuric acid with a mass concentration of 40% to the mother liquor I, control the reaction temperature at 100°C, and the stirring speed at 200r / min, cool down to 50°C after reacting for 1.0h, and then keep warm for crystallization After 2.0 hours, filter and separate, and wash the filter cake with water to obtain calcium sulfate whiskers and mother...
Embodiment 3
[0044] Phosphorus tailings and water are added to the slurry mixing tank to prepare a slurry with a solid content of 45%, and then the mixed reaction of phosphorus tailings slurry and 30% dilute nitric acid with a mass fraction of 30% is input to the upper and lower parts of the leaching tank simultaneously through a pump. The ratio of nitric acid to the sum of the molar amounts of CaO and MgO in phosphorus tailings is 2.05:1, and the reaction temperature is 95°C. After 1.5 hours of reaction, filter and separate to obtain filter residue I and mother liquor I, and filter residue I is used to make cement; Add ammonium sulfate to the mother liquor I with a molar ratio of 1:1, control the reaction temperature at 85°C, cool down to 40°C after reacting for 1.0h, then crystallize for 2.0h to filter and separate, the filter cake is washed with water and dried to obtain calcium sulfate whiskers and Mother liquor II circulates to decompose phosphorus tailings; after the mother liquor has...
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