Treatment device and method for 2,3-dichloropyridine production wastewater
A technology for the production of wastewater and treatment devices, which is applied in water/sewage treatment, natural water treatment, water treatment parameter control, etc. It can solve the problems of unfavorable amplification treatment, complicated treatment methods, and high pressure on environmental protection of the three wastes, and achieve simplified wastewater treatment process , The treatment process is simple and efficient, and the effect of reducing the cost of wastewater treatment
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Embodiment 1
[0025] Such as figure 1 , a treatment device for wastewater produced by 2,3-dichloropyridine, comprising a wastewater storage tank 1, a mixer 3, a hydrogen peroxide storage tank 4, an ultrasonic catalytic reactor 6, a heat exchanger 7, a photocatalytic reaction tower 8, and a wastewater storage tank The liquid outlet pipe of tank 1 is connected to the liquid inlet end of metering pump 2, and the liquid outlet pipe of metering pump 2 is connected to the liquid inlet end of mixer 3, and the waste water in waste water storage tank 1 is pumped into mixer 3 by metering pump 2, and the mixer One of the liquid inlets of 3 is connected to the liquid outlet pipe of hydrogen peroxide storage tank 4, and a flowmeter 5 is installed on the liquid outlet pipe of hydrogen peroxide storage tank 4, and hydrogen peroxide storage tank 4 supplies hydrogen peroxide to mixer 3, and flowmeter 5 is used to measure the hydrogen peroxide The flow rate, the mixer 3 is connected to the ultrasonic catalyt...
Embodiment 2
[0031] 2,3-dichloropyridine production waste water treatment device specific implementation steps are as follows: 2,3-dichloropyridine distillation suction filtration waste water (COD5541ppm) in 4m 3 / h flow rate pumped into the mixer 3, 27% hydrogen peroxide at 0.5m 3 / h flow rate into the mixer 3, mixed with hydrogen peroxide to obtain a mixed solution, the mixed solution is injected into the ultrasonic catalytic reactor 6, the reaction temperature is 10°C, and the residence time of the mixed solution in the ultrasonic catalytic reactor 6 is 3h; The heat exchanger 7 is preheated to 35°C and enters the photocatalytic reaction tower 8. The mixed solution passes through the packing layer 13 for photocatalytic oxidation reaction, and the residence time in the photocatalytic reaction tower 8 is 20h; COD online monitor 9, COD is 323ppm, effluent directly enters and exits water storage tank 11, COD removal rate is 94.1%.
Embodiment 3
[0033] 2,3-dichloropyridine production waste water treatment device specific implementation steps are as follows: 2,3-dichloropyridine distillation suction filtration waste water (COD5541ppm) in 4m 3 / h flow rate pumped into the mixer 3, 27% hydrogen peroxide at 0.4m 3 / h flow rate into the mixer 3, mixed with hydrogen peroxide to obtain a mixed solution, the mixed solution is injected into the ultrasonic catalytic reactor 6, the reaction temperature is 10°C, and the residence time of the mixed solution in the ultrasonic catalytic reactor 6 is 3h; 6. The effluent is preheated to 35°C by the heat exchanger 7, and enters the photocatalytic reaction tower 8. The mixed solution passes through the packing layer 13 for photocatalytic oxidation reaction, and the residence time in the photocatalytic reaction tower 8 is 20h; the photocatalytic reaction tower 8. The effluent passes through the COD online monitor 9, and the COD is 351ppm. The effluent directly enters the water storage ta...
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