Nitrophosphate tail gas deamination device and nitrophosphate tail gas deamination process
A nitrophosphate fertilizer and tail gas technology, applied in the chemical industry, can solve the problems of great difficulty in deamination, achieve the effects of overcoming adverse effects, low fan power consumption, and stable and reliable operation
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Embodiment 1
[0020] Under normal temperature conditions, nitric acid solution is used as the absorbent, adjust the pH of the absorption solution to 3, the absorption solution is pumped and circulated, and dispersed into droplets through the spray device on the top of the tower. The measured droplet diameter is about 2.8mm, which is the same as that entering The ammonia-containing tail gas is subjected to countercurrent contact, and the spray density is controlled to be 89m 3 / (m 2 ﹒ h), the superficial gas velocity is 1.95m / s, the NH in the tail gas 3 It is removed by chemical reaction with nitric acid in the absorption liquid. After the purified tail gas passes through the mist eliminator to remove the entrained fine droplets, it is emptied by the induced draft fan, and the absorption liquid is discharged from the tower kettle. Absorption tower inlet NH 3 The content is 3000mg / m 3 , the export content is 419mg / m 3 , The deamination efficiency is 86%.
Embodiment 2
[0022] At room temperature, the nitric acid solution is used as the absorbent, adjust the pH of the absorption solution to 3, and the absorption solution is pumped to the spray device with a circulating pump, dispersed into droplets with a diameter of about 2.8mm, and countercurrently contacted with the ammonia-containing tail gas entering from the bottom of the tower to control The spray density is 140m 3 / (m 2 ﹒ h), the superficial gas velocity is 1.95m / s, the NH in the tail gas 3 Chemical reaction with nitric acid, NH 3 was removed. The tail gas after deamination is removed by the mist eliminator to remove the entrained liquid droplets, and then is drawn out by the induced draft fan to be emptied, and the kettle liquid is discharged out of the absorption system. Absorption tower inlet NH 3 The content is 3000mg / m 3 , the measured outlet ammonia content was 187 mg / m 3 , The deamination efficiency is 93.8%.
Embodiment 3
[0024]Control the inlet ammonia-containing tail gas temperature at 70°C, absorbing liquid temperature at 45°C, use nitric acid solution as the absorbent, adjust the absorbing liquid pH=3, and circulate the pump to transport the absorbing liquid to the spray device for dispersion. The droplet diameter is about 2.8mm, which is the same as that from The ammonia-containing tail gas entering the bottom of the tower is contacted in countercurrent, and the spray density is controlled to be 140m 3 / (m 2 ﹒ h), the superficial gas velocity is 1.95m / s, the NH in the tail gas 3 Chemically reacts with nitric acid and is removed. After the purified exhaust gas is demistered by the demister, it is discharged by the induced draft fan, and the absorption liquid in the tower kettle is led out of the absorption system. Absorption tower inlet NH 3 The content is 3000mg / m 3 , the export content is 232 mg / m 3 , The deamination efficiency is 92.3%.
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