New technology of applying double-effect forced circulation concentration method in production of ammonium phosphate
A technology of forced circulation and production process, which is applied in the direction of phosphate, phosphorus oxyacid, etc., can solve the problems of multiple heating steps, complicated heating environment, difficult control of supersaturation changes, and short equipment operation cycle, so as to achieve the increase of equipment operation cycle , reduce the number and height of equipment used, and significantly increase production capacity
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Embodiment 1
[0023] Such as figure 1 Shown is a two-effect forced circulation concentration method applied to the new process of ammonium phosphate production:
[0024] a. dilute phosphoric acid (P 2 o 5 Content 23%) is forced to circulate between heater 1 and flash chamber 2, dilute phosphoric acid is heated to 70°C for flash evaporation, the gas-liquid phase is separated in the flash chamber, and the P in the liquid phase phosphoric acid is 2 o 5 Enter the reaction chamber 3 after the content is raised to 29%;
[0025] b. P in reaction chamber 3 2 o 5 Phosphoric acid with a content of 29% reacts with ammonia gas to form a monoammonium phosphate slurry with a neutralization degree of 1.02; the generated reaction heat concentrates the monoammonium phosphate slurry, making the monoammonium phosphate slurry P 2 o 5 content rose to 31%;
[0026] c. The 31% monoammonium phosphate slurry is forced to circulate between the heater 4 and the flash chamber 5 at a heating temperature of 1...
Embodiment 2
[0030] Such as figure 1 Shown is a two-effect forced circulation concentration method applied to the new process of ammonium phosphate production:
[0031] a. dilute phosphoric acid (P 2 o 5 Content 25%) is forced to circulate between the heater 1 and the flash chamber 2, dilute phosphoric acid is heated to 74°C for flash evaporation, the gas-liquid phase is separated in the flash chamber, and the P in the liquid phase phosphoric acid is 2 o 5 Enter the reaction chamber 3 after the content is raised to 27%;
[0032] b. P in reaction chamber 3 2 o 5 Phosphoric acid with a content of 27% reacts with ammonia gas to form a monoammonium phosphate slurry with a neutralization degree of 1.01; the generated reaction heat concentrates the monoammonium phosphate slurry, making the monoammonium phosphate slurry P 2 o 5 content rose to 34%;
[0033] c. The 34% monoammonium phosphate slurry is forced to circulate between the heater 4 and the flash chamber 5 at a heating temperat...
Embodiment 3
[0037] Such as figure 1 Shown is a two-effect forced circulation concentration method applied to the new process of ammonium phosphate production:
[0038] a. dilute phosphoric acid (P 2 o 5 Content 24%) is forced to circulate between the heater 1 and the flash chamber 2, dilute phosphoric acid is heated to 72°C for flash evaporation, the gas-liquid phase is separated in the flash chamber, and the P in the liquid phase phosphoric acid is 2 o 5 After the content is increased to 30%, it enters the reaction chamber 3;
[0039] b. P in reaction chamber 3 2 o 5 Phosphoric acid with a content of 30% and slag acid in the concentration section (P 2 o 5 content of 37%) and react with gas ammonia to form a monoammonium phosphate slurry with a neutralization degree of 0.99; the generated reaction heat concentrates the monoammonium phosphate slurry, increasing the P2O5 content of the monoammonium phosphate slurry to 32%;
[0040] c. The 32% monoammonium phosphate slurry is forc...
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