Method for producing calcium ammonium nitrate by using waste liquid produced in the production of ethylphosphorus aluminum
A technology of calcium ammonium nitrate and ethyl phosphorus aluminum, which is applied in the direction of nitrate fertilizer, application, nitrogen fertilizer, etc., to achieve the effect of simple operation, less investment in equipment, and bright colors
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Embodiment 1
[0024] Mix the collected waste liquid produced in the production of ethylphosphorus aluminum with 30% nitric acid in a weight ratio of 3:7 in a 1000L reactor to make a mother liquor. Add 400Kg of mother liquor into a 1000L reactor, divide 500Kg of phosphate ore tailings into three parts on average, first put a part of phosphate ore tailings into the reactor, start the reaction, generate a large amount of gas and release heat, add after the reaction is stable The second batch of phosphate ore tailings is reacted. After the reaction is stable, the third batch of phosphate ore tailings is added for reaction until no gas escapes, which is the end of the reaction, and then the reaction product is put into the crystallization tank to cool to the environment Temperature, with the ss-1000 type centrifuge, the crystallization is centrifuged and dehydrated to no liquid and thrown out to obtain 450 Kg of calcium ammonium nitrate. The liquid thrown out is calculated based on the compositio...
Embodiment 2
[0026] The collected waste liquid produced in the production of ethylphosphorus aluminum and nitric acid with a mass percentage of 68% were uniformly mixed in a 1000L reactor at a weight ratio of 7:3 to prepare a mother liquor. Add 500Kg of mother liquor into a 1000L reactor, crush 500Kg of phosphate ore tailings to 40μm and divide them into four parts on average. After the reaction is stable, add the second batch of phosphate ore tailings for reaction. After the reaction is stable, add the third batch of phosphate ore tailings for reaction. After the reaction is stable, add the fourth batch of phosphate ore tailings for reaction until no gas escapes. Then the reaction product is put into the crystallization tank and cooled to ambient temperature, and the crystal is centrifuged and dehydrated until no liquid is thrown out with a ss-1000 type centrifuge, and 480Kg of calcium ammonium nitrate is obtained, and the liquid thrown out is used to produce B The components contained in...
Embodiment 3
[0028] Mix the collected waste liquid produced in the production of ethylphosphorus aluminum with 50% nitric acid in a weight ratio of 4:6 in a 1000L reactor to make a mother liquor. Add 400Kg of mother liquor into a 1000L reactor, crush 500Kg of phosphate ore tailings to 75μm and divide them into four parts on average. After the reaction is stable, add the second batch of phosphate ore tailings for reaction. After the reaction is stable, add the third batch of phosphate ore tailings for reaction. After the reaction is stable, add the fourth batch of phosphate ore tailings for reaction until no gas escapes. Then the reaction product is put into the crystallization tank and cooled to ambient temperature, and the crystal is centrifuged and dehydrated until no liquid is thrown out with a ss-1000 type centrifuge to obtain 500Kg of calcium ammonium nitrate, and the liquid thrown out is used to produce B The components contained in the waste liquid produced by phosphorus and aluminu...
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