Membrane filtration-electrocatalysis treatment method for sewage
A sewage treatment method and electrocatalytic technology, applied in water/sewage treatment, water/sludge/sewage treatment, sterilization/microdynamic water/sewage treatment, etc., can solve the problems of high energy consumption and low efficiency, and achieve The effect of improving energy utilization efficiency and pollutant treatment efficiency and overcoming the shortcomings of electrocatalytic processes
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Embodiment 1
[0046] A tubular carbon membrane with an average pore size of 0.56 μm is used as the conductive porous membrane (anode), and stainless steel is used as the pressure shell and also serves as the cathode (counter electrode) to form a cross-flow filtration electrocatalytic membrane reactor. The depth of the effluent of a sewage treatment plant deal with. Set treatment conditions: transmembrane pressure difference 0.1MPa, membrane surface flow velocity 1.95~2.05m s -1 , water temperature 25 ~ 32 ℃, working voltage 5V.
[0047] Influent water quality (sewage) indicators are: yellowish, smelly, COD 60-320 (mg·L -1 ), ammonia nitrogen 4~27(mg·L -1 ), turbidity 18-155 (NTU), pH value 6-9.
[0048] The results show that under the condition of no electricity, the filtration flux is 0.04m 3 .m -2 .h -1 , The COD removal rate is 50.31%, the ammonia nitrogen removal rate is 75%, and the turbidity removal rate is 80%. After an electric field is applied, the permeation flux increases ...
Embodiment 2
[0050] A titanium membrane with a filtration accuracy of 0.2 μm is used as the conductive porous membrane (anode), and stainless steel is used as the pressure shell and doubles as the cathode (counter electrode) to form a cross-flow filtration electrocatalytic membrane reactor. The treatment conditions are set: transmembrane pressure difference 0.1MPa , membrane surface velocity 3.2m s -1 , the temperature is 20-28°C, the working voltage is 5V, and the raw water is simulated wastewater, wherein, the simulated wastewater contains 5% of fly ash with an average particle size of 2μm, and 30mg·L of phenol -1 , ammonia nitrogen 30mg·L -1 .
[0051] After treatment, the removal rate of fly ash is 100%, the removal rate of phenol is 83%, and the removal rate of ammonia nitrogen is 60%.
Embodiment 3
[0053] A tubular carbon membrane with an average pore diameter of 2 μm is used as the conductive porous membrane (anode), and stainless steel is used as the pressure shell and also serves as the cathode (counter electrode). The processing conditions are set: working voltage 3.2V, membrane surface flow rate 3m s -1 , the transmembrane pressure difference is 0.1MPa, and the simulated wastewater is treated, wherein, the simulated wastewater contains 500mg·L of phenol -1 .
[0054] After treatment, the removal rate of phenol was 89%.
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