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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[0029] Example 1
[0030] Magnetic coagulation was used to treat tannery wastewater. The pH, chroma, turbidity, COD, TOC, SS, and conductivity of the wastewater were 7.57, 550, 563, 1647mg / L, 206.4mg / L, 2150mg / L and 8.03mS / cm. PAC and PAM are used as coagulant and coagulant, and the dosage is 600 and 4mg / L respectively. The slow stirring rate is 50 rpm, and the fast stirring rate and time are 300 rpm and 20 s, respectively. The turbidity of the coagulated effluent 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 and hot sides is 20, 50 ℃ respectively, continuous operation for 24h, the effluent conductivity is 6μS / cm, and the product water flux is 14.23kg / m 2 .h, the removal rate of suspended solids, potassium, calcium, sodium, magnesium, sulfate, Cl, and COD are all higher than 97%, the conductivity of the produced water continues to decrease during two day...
Example Embodiment
[0031] Example 2
[0032] Using the above coagulation process to treat tannery wastewater, the coagulant and conditions are as in the above example, the magnetic seed is added 400mg / L, and the particle size of the magnetic seed is 200 meshes, which can significantly shorten the settling time, from the original 30min to 5min. The water turbidity is less than 1.5NTU. At the same time, the sludge output is 1 / 2. The magnetic coagulation product water is subjected to ceramic membrane microfiltration treatment. The ceramic membrane is made of alumina material with an average pore diameter of 0.1μm and a flux of 480kg / m 2 At .h, the transmembrane pressure difference will increase from 3kPa to 8kPa for two consecutive days. The turbidity of the product water is lower than 0.5NTU, and the color removal rate is 46%. After that, membrane distillation is used, and PVDF hydrophobic membrane is used. The temperature of the cold and hot sides is 20 and 50℃ respectively, and the water flux is ...
Example Embodiment
[0033] Example 3
[0034] The tannery wastewater after magnetic coagulation in Example 2 is used for ceramic membrane treatment. The ceramic membrane is a composite material of alumina and zirconia, and the membrane pore size is 0.1 μm. Operating flux is 480kg / m 2 .h, using continuous operation conditions of 1h and 1min backflushing, which can achieve significant control of membrane fouling. After running for two consecutive days, the transmembrane pressure difference is only 4.5kPa. Ceramic membrane water production is not affected by the ceramic membrane pressure, and the water turbidity is less than 0.5NTU. Afterwards, membrane distillation is used, the hydrophobic membrane is PVDF-CTFE, the temperature of the hot and cold sides is 20, 65℃, and the water flux is 21.37kg / m 2 .h, the conductivity significantly decreased to 9μS / cm in the first 50h of continuous operation, and then slowly increased, and the conductivity of the water produced during continuous 400h operation was l...
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