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Deep Treatment of Ammonia Nitrogen Tannery Wastewater by an Electro-Fenton System

机译:电-Fenton系统深度处理氨氮制革废水

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The effect of an Electro-Fenton system on the deep treatment of ammonia nitrogen (NH3-N) and corresponding removal rate was investigated in this article. By using simulated ammonia nitrogen wastewater, it included a Cl- concentration of 3000 mg/L, SO42- concentration of 100 mg/L according to conventional leather wastewater conditions. Furthermore, Cl- and SO42- can be used as supporting electrolyte. After pretreatment, the ammonia nitrogen concentration kept about 100 mg/L. The optimal treatment conditions of Electro-Fenton system were obtained throughout single factors experiments. The current density was 150 A/m(2), the reaction time was 30 min, the plate spacing distance was 40 mm, and the reaction temperature was adjusted to 40 degrees C. After flocculation treatment of leather wastewater, the ammonia nitrogen concentration was 142.11 mg/L, and the tanning wastewater was further treated with an Electro-Fenton system. The final ammonia nitrogen concentration was 11.23 mg/L, which meets the first-level wastewater discharge standard. The removal rate was 92.10%, which indicated that the Electro-Fenton system is one kind of clean, feasible and sustainable treatment method for the deep treatment of ammonia nitrogen in tannery wastewater.
机译:本文研究了电子芬顿体系对氨氮(NH3-N)深度处理和相应去除率的影响。通过使用模拟氨氮废水,根据常规皮革废水条件,它的Cl-浓度为3000 mg / L,SO42-浓度为100 mg / L。此外,Cl-和SO42-可用作支撑电解质。预处理后,氨氮浓度保持在约100 mg / L。通过单因素实验获得了电子芬顿系统的最佳处理条件。电流密度为150 A / m(2),反应时间为30 min,板间距为40 mm,反应温度调节至40°C。皮革废水的絮凝处理后,氨氮浓度为142.11 mg / L,制革废水用Electro-Fenton系统进一步处理。最终氨氮浓度为11.23 mg / L,符合一级废水排放标准。去除率为92.10%,表明Electro-Fenton系统是一种清洁,可行,可持续的深度处理制革废水中氨氮的方法。

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