Control method for granularity of potassium nitrate product produced through double decomposition
The technology of a metathesis method and a control method is applied in the field of particle size control of potassium nitrate products by metathesis method, can solve the problems of unstable product purity, uneven crystal particle size, and high operational requirements, and achieves reduction of nucleation amount, uniform particle size, guaranteeing The effect of product quality
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Embodiment 1
[0018] Example 1 A method for controlling the particle size of potassium nitrate product by double decomposition method, comprising the following steps:
[0019] ⑴ Potassium chloride and ammonium nitrate by K + / NH 4 + =0.9 molar ratio into the metathesis tank, while the circulating mother liquor and washing water are also put into the metathesis tank, mixed to form a slurry with a solid content of 50%, and then the temperature is raised according to the conventional method for the metathesis reaction to obtain the reaction slurry.
[0020] ⑵The reaction slurry is sent to the potassium nitrate cooling crystallization reactor, and the temperature is lowered from 120°C to 80°C, and the residence time is 0.5 hours. After 0.5 hour, a potassium nitrate crystallizer underflow slurry was obtained.
[0021] (3) Import the underflow slurry of the potassium nitrate crystallizer into the cyclone to obtain the underflow of coarse granular potassium nitrate crystals and the feed liq...
Embodiment 2
[0024] Example 2 A method for controlling the particle size of potassium nitrate product by double decomposition method, comprising the following steps:
[0025] ⑴ Potassium chloride and ammonium nitrate by K + / NH 4 + = 1.1 molar ratio into the metathesis tank, and at the same time, the circulating mother liquor and washing water are also put into the metathesis tank, mixed to form a slurry with a solid content of 40%, and then the temperature is raised according to the conventional method to carry out the metathesis reaction to obtain the reaction slurry.
[0026] ⑵Send the reaction slurry into the first potassium nitrate cooling crystallization reactor, firstly cool down from 110°C to 80°C, stay for 0.5 hours, and then enter the second potassium nitrate cooling crystallization reactor from 80°C to 30°C , after a residence time of 0.5 hour, the potassium nitrate crystallizer underflow slurry was obtained.
[0027] (3) Import the underflow slurry of the potassium nitr...
Embodiment 3
[0030] Example 3 A method for controlling the particle size of potassium nitrate product by double decomposition method, comprising the following steps:
[0031] ⑴ Potassium chloride and ammonium nitrate by K + / NH 4 + =1.3 molar ratio into the metathesis tank, while the circulating mother liquor and washing water are also put into the metathesis tank, mixed to form a slurry with a solid content of 40%, and then the temperature is raised according to the conventional method for the metathesis reaction to obtain the reaction slurry.
[0032] ⑵The reaction slurry is sent to the first potassium nitrate cooling crystallization reactor, and the temperature is lowered from 100°C to 70°C, and the residence time is 0.6 hours, and then the temperature is lowered from 70°C to 25°C in the second potassium nitrate cooling crystallization reactor , After a residence time of 0.6 hour, the potassium nitrate crystallizer underflow slurry was obtained.
[0033] (3) Import the underflow...
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