Production method and system of diammonium orthophosphate
A production method and technology of diammonium phosphate, applied in the direction of ammonium orthophosphate fertilizer, phosphate, phosphorus oxyacid, etc., can solve the problems of inconsistent product particle size, nitrogen content less than 18%, unrounded appearance, etc. , to achieve the effect of low moisture content, uniform particle size, and not easy to agglomerate
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Embodiment 1
[0042] see figure 1 , Embodiment 1 provides a kind of production method system of diammonium phosphate, comprising ammonia station, phosphoric acid storage tank, washing system, crusher, hot blast stove, return material structure, neutralization tank, tubular reactor, granulator, Dryer, sorting sieve, fluidized bed cooler, swinging sieve and packaging structure, etc. Among them, the ammonia station is connected with the neutralization tank, the tubular reactor and the granulator; The outlet of the material (greater than 4mm), the crusher and the inlet of the return structure are connected in sequence, the outlet of the fine material (less than 2mm) of the sorting sieve is connected with the inlet of the return structure, the outlet of the qualified material (2-4mm) of the sorting sieve, The fluidized bed cooler and the swinging screen are connected to the packaging structure in sequence, the outlet of the return structure is connected to the return inlet of the granulator, an...
Embodiment 2
[0045] see figure 1 , embodiment 2 provides a kind of production method of diammonium phosphate, comprises the following steps:
[0046] (1) Pre-neutralization: the concentrated phosphoric acid from the phosphoric acid storage tank and the washing liquid from the washing system are added to the neutralization tank, and react with the ammonia from the ammonia station. The reaction temperature is 115°C and the amino acid ratio is 0.001t / m 3 , the neutralization degree at the end point is 0.55, the slurry density is 1.51g / cm³, the water content of the slurry is 18%, the volume of the washing liquid used in this step is 1 / 3 of the neutralization tank, and the concentration of the washing liquid is 1.46g / cm³ , and the degree of neutralization is 0.55.
[0047] (2) Neutralization: The pre-neutralization slurry obtained in step (1) is passed into a tubular reactor containing 1 / 2 volume (from the washing system) of washing liquid, and reacts with ammonia from the ammonia station, and...
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