A method for three-dimensional pulse electrolytic removal of ammonia nitrogen
A technology of pulse electrolysis and ammonia nitrogen, applied in chemical instruments and methods, water/sludge/sewage treatment, water/sewage treatment, etc., to achieve the effects of high economic benefits, improved mass transfer intensity, and wide source of raw materials
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Embodiment 1
[0032] A method for removing ammonia nitrogen by three-dimensional pulse electrolysis is characterized in that it includes several sets of processing systems.
[0033] Such as figure 1 The single treatment system shown includes: power supply 1 , cathode and anode plates 2 , particle electrodes 3 , electrolytic tank 4 , constant current circulation pump 5 and circulation water container 6 .
[0034] The electrolytic cell 4, the constant-current circulating pump 5 and the circulating water container 6 are connected through relevant pipelines to form a closed loop. The constant current circulation pump 5 is connected to the water inlet end of the electrolytic cell 4 . The circulating water container 6 is connected to the water outlet of the electrolytic cell 4 .
[0035] Several groups of cathode and anode plates 2 are arranged inside the electrolytic cell 4 . The cathode and anode plates 2 are perpendicular to the water inlet direction and the water outlet direction of the el...
Embodiment 2
[0040] A method for three-dimensional pulse electrolytic removal of ammonia nitrogen, characterized in that, using the system in Example 1, the following steps are carried out:
[0041] 1) Configure simulated ammonia nitrogen wastewater: the concentration range of ammonium sulfate is 318.6 g / L, the concentration range of sodium sulfate is 10 g / L, and the concentration range of sodium chloride is 125 mg / L;
[0042] 2) The distance between the plates in the electrolytic cell 4 is 5 mm, the total filling capacity of coconut shell activated carbon is 130 g, and the current density is 109.65 mA / cm 2 , the constant flow pump flow range is 500-1000 mL / h, measure 650 mL of simulated distribution water in step 1), load pulse current electrolysis for 300 min, and the removal rate of ammonia nitrogen in the simulated distribution water reaches 78.11%;
[0043] The anode plate is meshed titanium plated ruthenium iridium (size: 57 mm*76 mm*1 mm), the cathode plate is mesh stainless steel (...
Embodiment 3
[0046] A method for three-dimensional pulse electrolytic removal of ammonia nitrogen, characterized in that, using the system in Example 1, the following steps are carried out:
[0047] 1) Configure the simulated ammonia nitrogen wastewater: the ammonium sulfate concentration range is 318.6 g / L, the sodium sulfate concentration range is 10 g / L, and the sodium chloride concentration range is 155 mg / L;
[0048] 2) The distance between the plates in the electrolytic cell 4 is 5 mm, the total filling capacity of coconut shell activated carbon is 130 g, and the current density is 109.65 mA / cm 2 , the constant flow pump flow range is 500-1000 mL / h, measure 650 mL of the simulated distribution water in step 1), load pulse current electrolysis for 300 min, and the removal rate of ammonia nitrogen in the simulated distribution water reaches 98.01%;
[0049] The anode plate is meshed titanium plated ruthenium iridium (size: 57 mm*76 mm*1 mm), the cathode plate is mesh stainless steel (s...
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