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Simultaneous Removal of COD and Ammonia Nitrogen Using a Novel Electro-Oxidation Reactor: A Technical and Economic Feasibility Study

机译:使用新型电氧化反应器同时去除COD和氨氮的技术和经济可行性研究

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A novel industrial-scale electro-oxidation device was built for simultaneous removal of ChemicalOxygen Demand (COD) and ammonia nitrogen in wastewater. The specific currents had a strong3 effect on removal rate and total current efficiency. At a specific current of 1440 A/m and electrolysistime of 40min, the concentrations of COD and ammonia nitrogen in effluent decreased from 128.75mg/L and 69.18 mg/L to 50.0 mg/L and 5.0 mg/L, respectively. The stepping control for the specificcurrent is useful for saving energy, and total current efficiency increased from 57.61% to 69.05% in3 response to use this stepping control model. The energy consumption was 4.34 kWh/m , the total3 operation cost for one ton of effluent was about $0.574 and the specific capital cost was $420/m /d.These findings indicate that the electro-oxidation process is capable of simultaneously decomposingrefractory organics and ammonia nitrogen in wastewater.
机译:建立了一种新型的工业规模的电氧化装置,用于同时去除废水中的化学需氧量(COD)和氨氮。特定电流对去除率和总电流效率有很强的影响。在1440 A / m的比电流和40min的电解时间下,废水中的COD和氨氮浓度分别从128.75mg / L和69.18 mg / L降至50.0 mg / L和5.0 mg / L。特定电流的步进控制有助于节省能源,使用此步进控制模型后,总电流效率从57.61%提高到69.05%。能耗为4.34 kWh / m3,一吨废水的总运行成本约为0.574美元,单位资本成本为420美元/ m 2 / d,这些发现表明,电氧化过程能够同时分解难处理的有机物和氨废水中的氮。

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