A Design Method of Bed Electrode Reactor for Wastewater Treatment
A technology for wastewater treatment and design methods, applied in water/sewage treatment equipment, water/sewage treatment, chemical instruments and methods, etc., can solve the unproposed engineering design methods for reactor design, current efficiency and energy consumption prediction, and difficult industrialization Problems such as application, inability to accurately design industrial wastewater treatment structures or equipment
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Embodiment 1
[0093] Example 1: The waste water volume of an amino acid production company in Nanjing is 150m 3 / d, raw water chemical oxygen demand (COD) is 4500mg / L on average, and NaCl mass concentration is more than 3%; Carry out engineering design according to technical scheme of the present invention, adopt respectively IrO 2 / Ta 2 o 5 / Ti and stainless steel as the anode and cathode, when the COD removal rate is 90%, the design reaction time is 1.5h, and the required area of the anode is 42m 2 , the direct energy consumption is 6.8kW·h / m 3 . The predicted values of reaction time, anode area and energy consumption are basically consistent with the experimental values.
Embodiment 2
[0094] Embodiment 2: Salt content (NaCl and NaCl and Na 2 SO 4 ) mass concentration is above 5%, and the pollutants are biologically toxic; the flow rate is 50m 3 / d, the average COD is 5000mg / L. Ti material and SnO 2 / Sb 2 o 3 / Mn / Ti is used as cathode and anode respectively, and the designed reaction time is 2.5h and the anode area is 7m 2 The engineering experiments conducted under the condition of the water show that the treated water COD is 220mg / L, and the energy consumption is 13.8kW·h / m 3 It is completely consistent with the theoretical prediction value carried out by adopting the technical scheme of the present invention.
Embodiment 3
[0095] Example 3: The production wastewater of a phenolic resin production enterprise in Hebei is still as high as 10000mg / L or more after phenolic polycondensation treatment, the pH value is 1.0, and the salinity mass concentration is above 5%, but the water volume is small, only 12m 3 / d, the design result obtained by the technical solution of the present invention is: reaction time 4.5h, anode area 22m 2 , treatment energy consumption 21.9kW·h / m 3 ; Effluent COD720mg / L; through this design, the proportion is reduced to 1m 3 / d scales simultaneously with IrO 2 / Ta 2 o 5 / Ti and stainless steel are used as anode and cathode, and the energy consumption and water effluent effect are close to the level predicted by the theory of the present invention.
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