Method for producing broad-concentration phosphoric acid and clean plaster by middle-low grade phosphorus ore wet process
A low-grade, phosphoric acid technology, applied in phosphoric acid, phosphorus oxyacid, calcium/strontium/barium sulfate, etc., can solve the problems of difficult beneficiation, large phosphorus loss, large equipment, etc. rate increase effect
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Embodiment 1
[0035] The technological process of this embodiment is as attached figure 2 shown. P of a phosphate rock 2 o 5 The grade is 16-18%, and the phosphate rock is processed into a powder whose 80% passes through a 0.125mm (120 mesh) sieve. Add 1000 parts of phosphate rock powder into the semi-water tank R1 for acidolysis. The operating conditions of the acidolysis reaction are: temperature 95-105°C, liquid-solid ratio 4-6, phosphoric acid concentration 37-42%P 2 o 5 , The reaction time is 1 to 3 hours. The acid-lysis slurry after the reaction enters the separator S1 for solid-liquid separation, and the obtained clear liquid enters the crystallization tank R2, and sulfuric acid is added to carry out the crystallization reaction. The crystallization operating conditions are: control SO 3 The concentration is 15-65g / L, the temperature is 100-110°C, and the crystallization reaction is 3-6 hours. After sufficient crystallization reaction, the slurry is separated through a vacuum ...
Embodiment 2
[0037] The process flow of this embodiment is shown in Figure 3. The grade of a certain phosphate rock is 22~28WT%P 2 o 5 . The particle size of the phosphate rock powder is 80% passing through a 0.075mm (200 mesh) sieve. Add 1000 parts of phosphate rock powder, enter the semi-water tank R1 for acidolysis, add sulfuric acid during the acidolysis process, the operating conditions of the acidolysis reaction are: temperature 95-105°C, liquid-solid ratio 5-8, phosphoric acid concentration 40-45WT% P 2 o 5 , control SO 3 The concentration is 10-20g / L, and the reaction time is 1-2 hours. The reacted acidolysis slurry enters the separator S1 for solid-liquid separation. The clear liquid obtained enters the crystallization tank R2, and sulfuric acid is added to carry out the crystallization reaction. The operating conditions of the crystallization reaction are: control SO 3 The concentration is 10-45g / L, the temperature is 100-110°C, and the crystallization reaction is 2-5 hou...
Embodiment 3
[0039] The technological process of this embodiment is as attached figure 2 shown. P of a phosphate rock 2 o 5 The grade is 16-18%, and the phosphate rock is processed into a powder whose 80% passes through a 0.125mm (120 mesh) sieve. Add 1000 parts of phosphate rock powder into the semi-water tank R1 for acidolysis. The operating conditions of the acidolysis reaction are: temperature 95-105°C, liquid-solid ratio 4-7, phosphoric acid concentration 37-42%P 2 o 5 , The reaction time is 1 to 3 hours. The acidolysis slurry after the reaction enters the separator S1, and uses it to separate the solid phase, and the obtained clear liquid enters the crystallization tank R2, and sulfuric acid is added to carry out the crystallization reaction. The operating conditions of the crystallization reaction are: control SO 3 The concentration is 15-65g / L, the temperature is 70-85°C, and the crystallization reaction takes 2-6 hours. After sufficient crystallization reaction, the slurry ...
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