Method for treating ammonium salt containing wastewater
A treatment method and wastewater technology, applied in multi-stage water treatment, water/sewage treatment, natural water treatment, etc., can solve the problems of low cost, high cost of wastewater treatment, and only mixed salt crystals can be obtained
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Embodiment 1
[0129] Such as figure 1 As shown, the wastewater containing ammonium salt (containing NaCl 130g / L, Na 2 SO 4 26g / L, NH 4 Cl 40g / L, (NH 4 ) 2 SO 4 8.1g / L, pH 6.5) with 5.859m 3 The speed of / h is sent into the pipeline of the treatment system, and the sodium hydroxide aqueous solution that imports concentration is 45.16 mass % in the pipeline is carried out the pH value adjustment for the first time, by the first pH value measuring device 61 (pH meter) after adjusting The pH value is monitored (the measured value is 9.0); wherein, a part of the waste water containing ammonium salt is passed through the first circulation pump 71 at 5.0m 3 The speed of / h mixes with the second mother liquor that the ninth circulating pump 79 returns to obtain waste water to be treated (wherein Cl - The concentration of SO is 3.737mol / L, SO 4 2- The concentration is 0.197mol / L, Cl - / SO 4 2- The molar ratio is 18.97), and then a part of the waste water to be treated is sent to the fir...
Embodiment 2
[0137] According to the method of embodiment 1, carry out the treatment containing ammonium salt waste water, difference is: to containing NaCl 68g / L, NaCl 2 SO 4 68g / L, NH 4 Cl 25g / L, (NH 4 ) 2 SO 4 25.4g / L, pH 6.3 wastewater containing ammonium salts, the feed volume is 6.84m 3 / h; part of the waste water in 5.0m 3 Cl - and SO 4 2- The molar ratio is 10.848; The concentration of NaCl in the wastewater to be treated obtained by mixing the rest of the ammonium-containing salt wastewater with the first mother liquor in the first mother liquor tank 53 is 237.85g / L, NaCl 2 SO 4 The concentration is 71.39g / L.
[0138] The evaporation temperature is 100°C, the pressure is -22.83kPa, and the evaporation volume is 5.530m 3 / h; the temperature of cooling treatment is 20°C, and the time is 65min; the temperature of cooling and crystallization is 0°C, and the time is 120min.
[0139] The first solid-liquid separation device 91 obtains water content per hour and is 755.64 kg...
Embodiment 3
[0143] Carry out the treatment of waste water containing ammonium salt according to the method of embodiment 1, difference is: to containing NaCl 50g / L, NaCl 2 SO 4 100g / L, NH 4 Cl 21g / L, (NH 4 ) 2 SO 4 42.69g / L, pH 6.7 wastewater containing ammonium salt, the feed amount is 9.39m 3 / h; part of the wastewater containing ammonium salt in 5.0m 3 Cl - and SO 4 2- The molar ratio is 11.640; The concentration of NaCl in the wastewater to be treated obtained by mixing the rest of the ammonium-containing salt wastewater with the first mother liquor in the first mother liquor tank 53 is 224.49g / L, NaCl 2 SO 4 The concentration is 62.84g / L. The temperature of the wastewater to be treated after heat exchange by the second heat exchange device 32 is 105°C.
[0144] The evaporation temperature is 110°C, the pressure is 11.34kPa, and the evaporation volume is 5.999m 3 / h; the temperature of cooling treatment is 25°C, and the time is 60min; the temperature of cooling and crysta...
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