节点文献

混凝—铁碳微电解—次氯酸钠氧化处理高氮废水

Treatment of high nitrogen wastewater by coagulation-iron carbon microelectrolysis-sodium hypochlorite oxidation process

  • 推荐 CAJ下载
  • PDF下载
  • 不支持迅雷等下载工具,请取消加速工具后下载。

【作者】 黄雷刘叶芳乐孝楠黄瑞敏

【Author】 HUANG Lei;LIU Yefang;LE Xiaonan;HUANG Ruimin;School of Environment and Energy,South China University of Technology;Key Laboratory of Pollution Control and Ecosystem Restoration in Industy Clusters,Ministry of Education;

【通讯作者】 黄瑞敏;

【机构】 华南理工大学环境与能源学院工业聚集区污染控制与生态修复教育部重点实验室

【摘要】 某印染工业园内的印花废水水量波动大,导致综合污水处理厂氮负荷高。采用混凝—铁碳微电解—次氯酸钠氧化组合工艺对该高氮废水进行处理。实验结果表明,在不调节初始 pH、硫酸亚铁与聚丙烯酰胺投加量分别为 400、15 mg/L 的条件下,混凝阶段的 COD 去除率达到 83.12%。在初始 pH 为 4、铁碳质量比为 1∶1、铁投加量为60 g/L、气水比为 5∶1、HRT 为 120 min 的条件下,对混凝出水进行铁碳微电解,出水 pH 升至 6.91,COD 和 NO3--N 的去除率分别为 50.26%、53.66%,NH4+-N 为 NO3--N 的主要还原产物。用次氯酸钠氧化法处理微电解出水,未调节初始pH、次氯酸钠与总凯氏氮质量比为 8.5∶1、反应时间为 30 min 时,TN、NH4+-N 的去除率分别为 88.56% 、97.75% 。经该组合工艺间歇处理后,出水 COD≤55 mg/L、TN≤14 mg/L、NH4+-N≤1 mg/L,可达到《纺织染整工业水污染物排放标准》(GB 4287—2012)表 2 的直接排放要求。经核算,该工艺的药剂成本为 5.09 元/t。

【Abstract】 In order to solve the problem of high nitrogen load caused by large fluctuation of wastewater in a printing and dyeing industrial park,a combined coagulation-iron carbon microelectrolysis-sodium hypochlorite oxidation process was used to treat the high nitrogen wastewater. The experimental results showed that the COD removal rate in coagulation stage reached 83.12% under the conditions of no adjustment of initial pH,ferrous sulfate and polyacrylamide dosage of 400 and 15 mg/L,respectively. Under the conditions of initial pH of 4,iron-carbon mass ratio of 1∶1,iron dosage of 60 g/L,gas-water ratio of 5∶1 and HRT of 120 min,iron-carbon microelectrolysis was applied to the coagulation effluent. The effluent pH increased to 6.91,and the removal rates of COD and NO3--N were50.26% and 53.66%,respectively,with NH4+-N as the main reduction product of NO3--N. The microelectrolysis effluent was treated with sodium hypochlorite. Under the conditions of no adjustment of initial pH,sodium hypochlorite to total Kjeldahl nitrogen mass ratio of 8.5∶1 and reaction time of 30 min,the removal rates of TN and NH4+-N were 88.56% and 97.75%,respectively. After intermittent treatment of combined process,the effluent COD≤55mg/L,TN≤14 mg/L and NH4+-N≤1 mg/L,met the direct discharge requirements in Table 2 of the Discharge standards of water pollutants for dyeing and finishing of textile industry(GB 4287—2012). After calculating,the cost of chemical agent of the process is 5.09 Yuan per ton.

  • 【文献出处】 工业水处理 ,Industrial Water Treatment , 编辑部邮箱 ,2022年04期
  • 【分类号】X791
  • 【被引频次】1
  • 【下载频次】284
节点文献中: 

本文链接的文献网络图示:

本文的引文网络