Combined process for advanced treatment of high-concentration and high-salt industrial wastewater
A technology for industrial wastewater and advanced treatment, applied in water/sewage treatment, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc. The effect of sludge moisture content, volume reduction, high chemical stability
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Embodiment 1
[0030] Using magnetic coagulation to treat tannery wastewater, the pH, chroma, turbidity, COD, TOC, SS, and conductivity of the wastewater are 7.57, 550, 563, 1647mg / L, 206.4mg / L, 2150mg / L and 8.03mS / cm. PAC and PAM are used as coagulant and coagulant aid, and the dosage is 600 and 4mg / L respectively. Slow stirring speed is 50rpm, fast stirring speed and time are respectively 300rpm and 20s. The turbidity of coagulated water is lower than 2.5NTU. The coagulation product water is directly subjected to membrane distillation treatment, using PVDF hydrophobic membrane, the temperature of the cold side and the hot side are 20, 50 ℃, and the continuous operation is 24 hours. 2 .h, the removal rates of suspended solids, potassium, calcium, sodium, magnesium, sulfate, Cl, and COD were all higher than 97%, the conductance of the product water continued to decrease during two days of continuous operation, and the membrane flux attenuation rate was 5%.
Embodiment 2
[0032] Using the above coagulation process to treat tannery wastewater, the coagulant and conditions are as in the above example, adding 400 mg / L of magnetic seeds, and the particle size of the magnetic seeds is 200 mesh, which can significantly shorten the settling time from 30 minutes to 5 minutes, and produce The water turbidity is lower than 1.5NTU. At the same time, the sludge output is 1 / 2 of the original. The water produced by magnetic coagulation is subjected to ceramic membrane microfiltration treatment. The ceramic membrane is made of alumina material, the average pore size of the membrane is 0.1μm, and the flux is 480kg / m 2 The transmembrane pressure difference increased from 3kPa to 8kPa during continuous operation for two days at .h. The turbidity of the product water is lower than 0.5NTU, and the color removal rate is 46%. Afterwards, membrane distillation treatment was adopted, using PVDF hydrophobic membrane, the temperatures of the cold and hot sides were 20...
Embodiment 3
[0034] The tannery wastewater after magnetic coagulation in Example 2 is used for ceramic membrane treatment, the ceramic membrane is made of alumina and zirconia composite material, and the membrane pore diameter is 0.1 μm. The operating flux is 480kg / m 2 .h, using the continuous operation condition of running for 1h and backflushing for 1min, significant control of membrane fouling can be achieved. After two days of continuous operation, the transmembrane pressure difference is only 4.5kPa. The water produced by the ceramic membrane is not affected by the pressure of the ceramic membrane, and the turbidity of the produced water is lower than 0.5NTU. Afterwards, membrane distillation is used, the hydrophobic membrane is PVDF-CTFE, the temperature of the cold side and the hot side are 20 and 65°C respectively, and the flux of the produced water is 21.37kg / m 2 .h, the conductance dropped significantly to 9μS / cm in the first 50h of continuous operation, and then increased slow...
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