A method for rapid removal of ammonia nitrogen from urban sewage plant effluent by electrochemically coupled zeolite adsorption
An urban sewage and electrochemical technology, applied in electrochemical water/sewage treatment, adsorbed water/sewage treatment, etc., can solve the problems of high cost, secondary pollution, complicated ammonia nitrogen operation and operation, achieve good running time and save electricity , the effect of reducing costs
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specific Embodiment approach 1
[0018] Specific implementation mode one: combine figure 1 As shown, the method for quickly removing ammonia nitrogen from the effluent of urban sewage plants by electrochemically coupling zeolite adsorption in this embodiment is carried out in the following steps:
[0019] 1. The effluent from the urban sewage treatment plant is collected and enters the storage tank 1;
[0020] 2. The effluent water from the storage tank 1 enters the coupled electrochemical reactor 3 filled with zeolite 4 through the peristaltic pump 2, starts the power supply 5, and enters the water from the bottom to the top, and enters from the cathode side, and overflows from the anode side. Ensure maximum contact between ammonia nitrogen and zeolite and plate;
[0021] 3. Cl in the effluent water in the coupled electrochemical reactor 3 - Oxidized by electrons generated by the anode to Cl 2 , the generated Cl 2 Contact with aqueous solution to generate HOCl or OCl - , HOCl or OCl - As a strong oxida...
specific Embodiment approach 2
[0029] Specific embodiment 2: The difference between this embodiment and specific embodiment 1 is that the electrode anode coupled to the electrochemical reactor 3 in step 2 is coated with RuO on the surface. 2 , IrO 2 and SnO 2 The multi-metal composite Ti electrode, the electrode cathode is a Ti mesh. Other steps and parameters are the same as those in Embodiment 1.
specific Embodiment approach 3
[0030] Specific embodiment three: the difference between this embodiment and specific embodiment one or two is that the circulation flow in the coupling electrochemical reactor 3 in step two is 100mL / min, and the electrochemical current density is 3mA / cm 2 , The hydraulic retention time is 30min. Other steps and parameters are the same as those in Embodiment 1 or Embodiment 2.
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