A method for producing diammonium phosphate from phosphate rock with high impurity content
A technology for producing diammonium phosphate and impurity content, applied in the direction of phosphate, phosphorus oxyacid, etc., can solve the problem of low effective phosphorus, achieve the effect of strong adaptability and realize large-scale industrial production
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Embodiment 1
[0036] Take 1000.0g of wet dilute phosphoric acid (25%P 2 O 5 ), filter out the phosphogypsum, transfer the filtrate to the sedimentation tank, add the impurity remover oxalic acid (H 2 C 2 O 4 ) 5.0%, set the temperature in the settling tank to be 60 ° C, get the supernatant and concentrate it until the concentrated solution contains P 2 O 5 The concentration of the phosphoric acid is 44-47%, adding aluminum phosphate, adjusting the viscosity to 33-38mPa·s, the obtained concentrated phosphoric acid is transported to the tubular reactor, and reacts with ammonia gas in the tubular reactor to generate slurry, adjust the slurry The degree of neutralization was 1.56, and the slurry was sprayed on the master batch in the granulator, and the degree of neutralization was increased to 1.84 through secondary ammoniation to generate diammonium phosphate particles. The analysis indicators are: total nutrient% = 63.9, available phosphorus% = 46.5, total N% = 17.8, H 2 0%=2.0.
Embodiment 2
[0038] Take 1000.0g of wet dilute phosphoric acid (25%P 2 O 5 ), filter out the phosphogypsum, transfer the filtrate to the sedimentation tank, add the impurity remover oxalic acid (H 2 C 2 O 4 ) 7.0%, set the temperature in the sedimentation tank to be 60 ° C, take the supernatant and concentrate it until the concentrated solution contains P 2 O 5 The concentration of the phosphoric acid is 44-47%, adding aluminum phosphate, adjusting the viscosity to 33-38mPa·s, the obtained concentrated phosphoric acid is transported to the tubular reactor, and reacts with ammonia gas in the tubular reactor to generate slurry, adjust the slurry The degree of neutralization was 1.56, and the slurry was sprayed on the master batch in the granulator, and the degree of neutralization was increased to 1.84 through secondary ammoniation to generate diammonium phosphate particles. The analysis indicators are: total nutrient% = 64.1, available phosphorus% = 46.3, total N% = 17.4, H 2 0%=2.1. ...
Embodiment 3
[0040] Take 1000.0g of wet dilute phosphoric acid (25%P 2 O 5 ), filter out the phosphogypsum, transfer the filtrate to the sedimentation tank, add the impurity remover oxalic acid (H 2 C 2 O 4 ) 10.0%, set the temperature in the sedimentation tank to be 60 ° C, take the supernatant and concentrate it to the concentration containing P 2 O 5 The concentration of the phosphoric acid is 44-47%, adding aluminum phosphate, adjusting the viscosity to 33-38mPa·s, the obtained concentrated phosphoric acid is transported to the tubular reactor, and reacts with ammonia gas in the tubular reactor to generate slurry, adjust the slurry The degree of neutralization was 1.56, and the slurry was sprayed on the master batch in the granulator, and the degree of neutralization was increased to 1.84 through secondary ammoniation to generate diammonium phosphate particles. The analysis indicators are: total nutrient% = 64.3, available phosphorus% = 46.4, total N% = 17.6, H 2 0%=2.3.
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