A method and production system for graded preparation of powdered ammonium and high-quality ammonium phosphate from phosphate rock
A high-quality, ammonium phosphate technology, applied in chemical instruments and methods, phosphate, solid separation, etc., can solve the problems of large price gap, unstable quality, large purchase of phosphate rock, etc., and achieve the goal of stable quality and improved quality Effect
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Embodiment 1
[0033] see Figure 1-3 , Embodiment 1 provides a kind of method for preparing powder ammonium and high-quality ammonium phosphate by classification of phosphate rock, the method comprises the following steps:
[0034] (1) Phosphate slurry with a density of 1.25-1.30 g / ml and a fineness of 100 mesh ≥ 90% is obtained by the ball mill 3, the slurry tank 4 and the primary cyclone 5. The taper at the bottom of the primary cyclone 5 is 30-45°.
[0035] (2) send the phosphate ore pulp obtained in step (1) to the secondary cyclone 1 for processing to obtain low-grade ore pulp (overflow, density is about 1.15 g / ml, P 2 O 5 The content of ore is less than 26.5%, the content of MgO is more than 3%) and high-grade pulp (sediment, density 1.65-1.70 g / ml, P 2 O 5 The content of MgO is more than 28.5%, the content of MgO is less than 4%), the processing pressure is 0.08-0.12MPa, and the taper of the bottom of the secondary cyclone 1 is 18-25°. The quality of the low-grade pulp usually o...
Embodiment 2
[0054] see Figure 1-3 , embodiment 2 provides a kind of phosphate rock classification to prepare the production system of powder ammonium and high-quality ammonium phosphate, and this system comprises:
[0055] The ore pulp preparation device is used to obtain phosphate ore pulp with a density of 1.25-1.30g / ml and a fineness of 100 mesh ≥90%. It is similar to the conventional structure, except that the indicators of the ore pulp need to be adjusted to suit the secondary cyclone 1.
[0056] The secondary cyclone 1 is used to classify the pulp output from the pulp preparation device to obtain high-grade pulp and low-grade pulp respectively, and the taper of the bottom is 18-25°. The secondary cyclone 1 is different from the primary cyclone 5, and the effect of grade separation can only be achieved under specific structure and feeding conditions. Specifically, the model of the secondary cyclone 1 in this embodiment is a FX250-GX×18 double-feed cyclone group, with 8 units runnin...
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