Zero-discharge cyclic utilization method for desulfurized wastewater of thermal power plant
A technology for thermal power plants and desulfurization wastewater, applied in gaseous effluent wastewater treatment, chemical instruments and methods, water/sewage treatment, etc., can solve the problems of flue system corrosion, limit the utilization of desulfurization wastewater in thermal power plants, etc., and achieve The effect of reducing pollution
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Embodiment 1
[0016] (1) A pH adjustment tank with an alkali addition pipeline and a pH meter, a sedimentation tank with an alkali addition pipeline, and an evaporator are sequentially installed at the outlet of the desulfurization wastewater of the thermal power plant to be treated. The pH adjustment tank with alkali adding pipeline and pH meter is made of commercially available 8mm thick carbon steel plate, with a volume of 30m 3 The alkali-adding pipeline of the pH adjustment tank adopts a commercially available PVC dosing pipe with a diameter of 20 mm, and inserts the pipe into the middle and lower part of the pH adjustment tank body; the pH meter of the pH adjustment tank adopts a commercially available American polymetron 9135 type pH meter. The tank body of the sedimentation tank is also cut from 8mm thick carbon steel plate, with a volume of 40m 3 , the alkali-adding pipeline of this settling tank also adopts a commercially available PVC dosing pipe with a diameter of 20mm, and ins...
Embodiment 2
[0021] Steps (1) to (3) are the same as in Example 1;
[0022] (4) Using a conventional method, determine the process data of the evaporator according to the increase in the boiling point of the desulfurization wastewater containing salt and the increase in the evaporation boiling point of the desulfurization wastewater. The desulfurization wastewater treated in step (3) is injected into the evaporator set up in step (1) for evaporation and concentration in the following three stages. In the first stage, the temperature is controlled at 98-100°C and takes 140 minutes; in the second stage, the temperature is controlled at 74-78°C and it takes 120 minutes; in the third stage, the temperature is controlled at 50-54°C and it takes 180 minutes to evaporate Condensed water with a salt content of 3-5‰ produced by concentration can be directly used as boiler make-up water or power plant circulating water make-up water.
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