Method for treating centrifuge mother liquor waste water from polychloroethylene production
A technology for centrifugal mother liquor and polyvinyl chloride, which is applied in biological water/sewage treatment, natural water treatment, sustainable biological treatment, etc., can solve the problems of high operating cost, increased operating cost, large waste water discharge, etc., and can reduce the operation cost. Costs, improved service life, and reduced emissions
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Embodiment 1
[0023] Embodiment 1: see figure 2 , shown in the figure is the flowchart of the first embodiment of the PVC centrifugal mother liquor wastewater treatment process of the present invention. PVC centrifugal mother liquid wastewater enters the plate heat exchanger, after the temperature of the wastewater drops from 85°C to 40°C, it enters the adjustment tank (400-500m3), and is mixed homogeneously in the adjustment tank, and the hydraulic retention time is 1-5 hours. The wastewater in the adjustment tank is pumped into the aeration tank for aerobic reaction, and a certain amount of nutrient salt is added to the aeration tank, urea and sodium phosphate are added according to the ratio of COD:N:P=100:1:0.3), so that The easily degradable organic matter in the wastewater is degraded by biological bacteria, and the hydraulic retention time is 12-36 hours. After the degradation, the wastewater flows into the coagulation air flotation system by itself. Add the coagulant polyaluminum ...
Embodiment 2
[0025] Example 2: see image 3 , shown in the figure is the flow chart of the second embodiment of the PVC centrifugal mother liquor wastewater treatment process of the present invention. PVC centrifugal mother liquid wastewater enters the cooling tower, after the temperature of the wastewater drops from 85°C to 30°C, it enters the regulating tank (400-500m3), and is mixed homogeneously in the regulating pool, and the hydraulic retention time is 1-5 hours. The wastewater in the adjustment tank is pumped into the aeration tank for aerobic reaction, and a certain amount of nutrient salt is added to the aeration tank, and urea and phosphoric acid are added according to the ratio of COD:N:P=100:2:0.1), so that the wastewater The easily degradable organic matter in the water is degraded by biological bacteria, and the hydraulic retention time is 12-36 hours. After that, the degraded waste water flows into the coagulation air flotation system by itself. Add the coagulant polyalumin...
Embodiment 3
[0027] Embodiment 3: see Figure 4 , shown in the figure is the flow chart of the third embodiment of the PVC centrifugal mother liquor wastewater treatment process of the present invention. PVC centrifugal mother liquid wastewater enters the cooling tower, after the temperature of the wastewater drops from 85°C to 15°C, it enters the regulating tank (400-500m3), and is mixed homogeneously in the regulating pool, and the hydraulic retention time is 1-5 hours. The wastewater in the adjustment tank is pumped into the aeration tank for aerobic reaction, and a certain amount of nutrient salt is added to the aeration tank. Urea and phosphoric acid are added according to the ratio of COD:N:P=100:3:0.4, so that the waste water The easily degradable organic matter is degraded by biological bacteria, and the hydraulic retention time is 12-36 hours. After the degradation, the waste water flows into the coagulation air flotation system by itself. Add 1g of coagulant polyacrylamide to th...
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