Method for producing feed grade dicalcium phosphate
A technology of monocalcium phosphate and production methods, which is applied in the direction of animal feed, animal feed, chemical instruments and methods, etc., can solve the problem of incomplete crystallization water of calcium hydrogen phosphate and calcium dihydrogen phosphate, large investment in phosphoric acid concentration equipment, and production process Process lengthening and other issues, to achieve the effect of advanced technology and product quality, improved biological potency, and complete crystallization water
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Embodiment 1
[0038] In the reaction tank, add 3095Kg of wet purification phosphoric acid (in P 2 o 5The calculated concentration is 39.7%), stir well, slowly add 888Kg of calcium carbonate under stirring, make it into calcium dihydrogen phosphate slurry, after neutralization reaction for 30 minutes, continue to slowly add lime milk 821Kg (water content 60%), continue to stir for 30 minutes after the gray milk is added, and transfer to the vibrating screen to separate the coarse particles. The slurry is sprayed from the transfer tank through the centrifugal spray pump to the spray plate, and dried with hot air with an inlet temperature of 400°C. The temperature of the tower is 90°C. After the material comes out of the bottom of the tower, it is sieved through a 2mm diameter sieve to obtain 2645Kg of monocalcium phosphate product. Its product quality indicators are as follows:
[0039] Total Phosphorus
Embodiment 2
[0041] Add 6138Kg of wet purification phosphoric acid (in P 2 o 5 The calculated concentration is 10.2%), stir well, slowly add 242Kg of calcium oxide under stirring, make it into calcium dihydrogen phosphate slurry, after neutralization reaction for 30 minutes, continue to slowly add lime milk 415Kg (water content 60%), continue to stir for 30 minutes after the gray milk is added, transfer to the vibrating screen to separate the coarse particles, the slurry is sprayed from the transfer tank through the centrifugal spray pump to the spray plate, and dried by hot air with an inlet temperature of 180°C. The temperature of the tower is 90°C. After the material comes out of the bottom of the tower, it passes through the rotary cylinder with the temperature of the air inlet at 600°C and the temperature of the air outlet at 70°C. Its product quality indicators are as follows:
[0042] Total Phosphorus
Embodiment 3
[0044] In the reaction tank, add 3742Kg of wet purification phosphoric acid (in P 2 o 5 Concentration is 33%), stir well, slowly add 1600Kg milk of lime (water content is 60%) under stirring, make adjustment into calcium dihydrogen phosphate slurry, after 30 minutes of neutralization reaction, continue to slowly add to the slurry Add 821Kg of lime milk (moisture content 60%), continue to stir for 30 minutes after adding lime milk, transfer to vibrating screen to separate coarse particles, the slurry is sent from the transfer tank to the spray plate through the centrifugal spray pump, and the inlet temperature is 750 ℃ hot air drying, the outlet temperature is 90℃, after the material comes out from the bottom of the tower, it is passed through a rotary cylinder with an air inlet temperature of 600℃ and an air outlet temperature of 70℃. Monodicalcium phosphate products. Its product quality indicators are as follows:
[0045] Total Phosphorus
PUM
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