Rotary kiln method phosphoric acid production system and production method with preheating and high temperature consolidation outside the kiln
A production system and rotary kiln technology, applied in phosphoric acid, phosphorus oxyacids, chemical instruments and methods, etc., can solve the problems of easy ring formation, high energy consumption and cost, difficult industrial production, and low strength of the coating layer. To achieve the effect of simple and compact overall structure, low production cost and improved economy
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Embodiment 1
[0053] Figure 1 to Figure 4 Shown the first embodiment of the rotary kiln method phosphoric acid production system of the present invention, including furnace gas circulation device 1, consolidation screening device 2, reduction and oxidation device 3 and hydration acid recovery device 4 , the consolidation screening device 2 includes a shaft furnace body 21, and the shaft furnace body 21 is provided with a screening assembly 22 in the inner cavity, and the screening assembly 22 divides the inner cavity of the shaft furnace body 21 into an upper consolidation cavity 23 and a The lower ash discharge chamber 24, the furnace gas circulation device 1 is communicated with the upper consolidation chamber 23, the upper consolidation chamber 23 receives external raw materials, and the upper consolidation chamber 23 is communicated with the reduction and oxidation device 3, and the reduction and oxidation device 3 and the hydration acid recovery device 4 Connected. When in use, the r...
Embodiment 2
[0070] like Figure 5 As shown, the second embodiment of the rotary kiln method phosphoric acid production system of the present invention, which is preheated and consolidated at high temperature outside the kiln, the production system is basically the same as the system embodiment 1, and the difference is only that: in this embodiment, the shaft furnace body 21 is set as a rectangular structure, and its inner cavity is provided with a rectangular cavity. Its structure is simple and reliable.
[0071] In this embodiment, the rectangular shaft furnace and its operating parameters are: the size of the shaft furnace: 3×4.2×3.6m, the temperature of the flue gas at the air inlet 28: 900~1000°C, and the temperature of the flue gas at the air outlet 26: 200~400°C ℃, pellet temperature at inlet 28: 200℃, pellet temperature at outlet 26: 900~1100℃, processing pellet volume: 30t / h, superficial gas velocity is 0.2~2m / s.
[0072] Method Example 1:
[0073] Figure 1 to Figure 6 Shown ...
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