...
首页> 外文期刊>Environmental Science: Water Research & Technology >The fate of dichloroacetonitrile in UV/Cl_2 and UV/ H_2O_2 processes: implications on potable water reuse
【24h】

The fate of dichloroacetonitrile in UV/Cl_2 and UV/ H_2O_2 processes: implications on potable water reuse

机译:UV / Cl_2和UV / H_2O_2工艺中二氯乙腈的命运:对饮用水回用的影响

获取原文
获取原文并翻译 | 示例
           

摘要

This study investigated the fate of DCAN in UV/Cl-2 and UV/H2O2 processes under the conditions relevant to potable water reuse (e.g., two pH values and three oxidant dosages). At pH 6 and an oxidant dosage of 500 M, the degradation of DCAN in the UV/Cl-2 process was attributed to UV photolysis (4.5%), HO--assisted hydrolysis (10.5%), nucleophilic attack by ClO- (32.2%), and oxidation by radicals (i.e., HO and Cl) (52.8%), while that in the UV/H2O2 process was mainly attributed to HO2- (32%) and HO (48%). In both processes, the DCAN degradation rates were higher with increasing solution pH from 5 to 6, because the increased HO--assisted hydrolysis and nucleophilic attack of DCAN surpassed the decreased radical oxidation of DCAN. The DCAN degradation was enhanced with increasing chlorine or H2O2 dosage from 100 to 1000 M, mainly due to the increased contribution from the nucleophilic attack. DCAN was mostly transformed into dichloroacetic acid (DCAA) through different pathways in the two processes. At the same pH and oxidant dosage conditions, the degradation rates of DCAN in the UV/Cl-2 process were higher than those in the UV/H2O2 process, due to the higher nucleophilic attack rates and radical oxidation rates in the former process. The cost of degrading 90% of DCAN using the UV/Cl-2 process is about 1/8 of that using the UV/H2O2 process, making the UV/Cl-2 process a more cost-effective UV-AOP in DCAN abatement for potable water reuse.
机译:这项研究调查了在与饮用水回用有关的条件下(例如两个pH值和三个氧化剂剂量)DCAN在UV / Cl-2和UV / H2O2工艺中的命运。在pH为6且氧化剂用量为500 M的情况下,DCAN在UV / Cl-2过程中的降解归因于UV光解(4.5%),HO辅助水解(10.5%),ClO-的亲核攻击(32.2 )和自由基的氧化(即HO和Cl)(52.8%),而UV / H2O2工艺中的氧化主要归因于HO2-(32%)和HO(48%)。在这两个过程中,随着溶液pH从5增加到6,DCAN降解速率都更高,这是因为HO辅助水解和DCAN亲核攻击的增加超过了DCAN自由基氧化的减少。随着氯或过氧化氢剂量从100 M增加到1000 M,DCAN降解得到增强,这主要是由于亲核攻击的贡献增加了。在两个过程中,DCAN主要通过不同途径转化为二氯乙酸(DCAA)。在相同的pH和氧化剂剂量条件下,由于前一过程中较高的亲核进攻速率和自由基氧化速率,UV / Cl-2过程中DCAN的降解速率高于UV / H2O2过程中的DCAN降解速率。使用UV / Cl-2工艺降解90%的DCAN的成本约为使用UV / H2O2工艺降解的成本的1/8,这使得UV / Cl-2工艺成为降低DCAN成本的更具成本效益的UV-AOP。饮用水回用。

著录项

  • 来源
  • 作者单位

    Hong Kong Univ Sci & Technol, Dept Civil & Environm Engn, Kowloon, Hong Kong, Peoples R China;

    Hong Kong Univ Sci & Technol, Dept Civil & Environm Engn, Kowloon, Hong Kong, Peoples R China;

    Hong Kong Univ Sci & Technol, Dept Civil & Environm Engn, Kowloon, Hong Kong, Peoples R China;

    Hong Kong Univ Sci & Technol, Dept Civil & Environm Engn, Kowloon, Hong Kong, Peoples R China;

  • 收录信息
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号