工业水处理 ›› 2015, Vol. 35 ›› Issue (7): 31-34. doi: 10.11894/1005-829x.2015.35(7).031

• 试验研究 • 上一篇    下一篇

臭氧氧化——化学沉淀法深度处理电镀含磷废水的研究

陈良1, 张炜铭1,2, 吕路1,2, 潘丙才1,2, 汪林2, 费正连2, 孙平1,2, 林原2, 虢清伟3   

  1. 1. 南京大学环境学院污染控制与资源化研究国家重点实验室, 江苏南京 210023;
    2. 江苏南大环保科技有限公司国家环境保护有机化工废水处理与资源化工程技术中心, 江苏南京 210046;
    3. 环境保护部华南环境科学研究所, 广东广州 510655
  • 收稿日期:2015-05-13 出版日期:2015-07-20 发布日期:2015-07-17
  • 作者简介:陈良(1991—),硕士。电话:18205186916,E-mail:job_cl@126.com。
  • 基金资助:

    国家水体污染控制与治理科技重大专项(2012ZX07206003);国家自然科学基金项目(51178214)

Study on the advanced treatment of electroplating phosphorus-containing wastewater by ozone oxidation-chemical precipitation process

Chen Liang1, Zhang Weiming1,2, Lü Lu1,2, Pan Bingcai1,2, Wang Lin2, Fei Zhenglian2, Sun Ping1,2, Lin Yuan2, Guo Qingwei3   

  1. 1. State Key Laboratory of Pollution Control & Resource Reuse, School of the Environment, Nanjing University, Nanjing 210023, China;
    2. State Environmental Protection Engineering Center for Organic Chemical Industrial Waste Water Disposal and Resources Reuse, Jiangsu NJU Environment Protection Technology Co., Ltd, Nanjing 210046, China;
    3. South China Institute of Environment Sciences, MEP, Guangzhou 510655, China
  • Received:2015-05-13 Online:2015-07-20 Published:2015-07-17

摘要:

以总磷为去除对象, 采用臭氧氧化—化学沉淀法联合工艺进行电镀含磷废水的处理。考察了臭氧投加量、臭氧反应时间、废水中总磷初始浓度、废水初始pH对非正磷酸盐氧化率的影响以及沉淀剂种类和浓度对沉淀效率的影响。实验结果表明, 经过臭氧氧化—化学沉淀法联合工艺的处理, 电镀废水总磷指标可以稳定达到《电镀污染物综合排放标准》(GB 21900—2008)表3中水污染物特别排放限值。

关键词: 电镀废水, 臭氧氧化, 含磷废水

Abstract:

Taking the total phosphorus as a removal target, the combined process, ozone oxidation-chemical prec- ipitation, has been used for removing phosphorus from real electroplating phosphorus-containing wastewater. The in- fluences of ozone dosage, oxidation reaction time, initial concentration of phosphorous, and initial pH on the oxida- tion rate of nonorthophosphate are investigated. And, the influences of the species and concentrations of precipitants on precipitation efficiency are also investigated. The results show that the total phosphorus index of phosphorus-co- ntaining wastewater can stably reach the water pollutant special discharge limit value specified in Table 3 of the Comprehensive Discharge Standard for Pollutants from Electroplating(GB 21900—2008), after it has been treated by the combined process, ozone oxidation-chemical precipitation.

Key words: electroplating wastewater, ozone oxidation, phosphorus-containing wastewater

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