Energy-saving method for recycling wastewater containing phenol and ammonia
A treatment method and wastewater recycling technology, which is applied in the directions of heating water/sewage treatment, degassed water/sewage treatment, extraction water/sewage treatment, etc., can solve the problem of high energy consumption, reduce capacity consumption, save consumption, and realize step-by-step The effect of comprehensive utilization
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Embodiment 1
[0061] (1) After the 75t / h waste water is transported from the gas-water separator, the suspended solids, tar and light oil are removed, the temperature is 40°C, and the pressure is 1.0MPa. The concentration is 5 g / L of phenol, 8.5 g / L of ammonia, 2.55 g / L of carbon dioxide, and 0.155 g / L of hydrogen sulfide.
[0062] (2) The phenol ammonia-containing wastewater coming over is divided into two streams: one stream directly enters the top of the tower at 20 t / h; the other stream is heated to 85° C. through the preheater 2 (13) and enters the middle of the deacidification tower (1).
[0063] (3) The deacidification tower is a plate tower. The operating pressure of the deacidification tower is 30kPa (gauge pressure), the temperature at the top of the tower is 40°C, and the bottom of the tower is 110°C. The bottom of the tower is heated by a reboiler (2), and the heat source is the heat released by the condensation of the crude gas at the top of the deamination tower (9). The cond...
example 1
[0071] (1) The ammonia concentration in the wastewater after deammonification is 100 mg / L.
[0072] (2) The mass concentration of ammonia water at the bottom of the ammonia concentration tower is 10%, and the ammonia concentration in the tail gas is 50 mg / m3.
[0073] (3) The mass concentration of the crude phenol product is 99%.
[0074] (4) The solvent consumption is 1.5kg / t waste water.
[0075] (5) The content of phenol in the treated wastewater is 250 mg / L
[0076] (6) The steam consumption of the device is 180kg steam / t waste water.
Embodiment 3
[0078]
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