4.7 Article

Disinfection byproduct formation resulting from settled, filtered, and finished water treated by titanium dioxide photocatalysis

期刊

CHEMOSPHERE
卷 117, 期 -, 页码 72-78

出版社

PERGAMON-ELSEVIER SCIENCE LTD
DOI: 10.1016/j.chemosphere.2014.05.073

关键词

Disinfection byproduct; Advanced oxidation; Titanium dioxide photocatalysis; Trihalomethane; Haloacetic acid; Organic matter characterization

资金

  1. National Science Foundation (NSF) Water 82 Environmental Technology Center at Arizona State University
  2. Arizona Water Institute
  3. Directorate For Engineering
  4. Div Of Industrial Innovation & Partnersh [1361815] Funding Source: National Science Foundation

向作者/读者索取更多资源

This study evaluated strategies targeting disinfection byproduct (DBP) mitigation using TiO2 photocatalysis with varying influent water quality. A Purifics Photo-CAT Lab reactor was used to assess total trihalomethane (TTHM) and haloacetic acid (HAA) formation as a function of photocatalytic treatment using water from a conventional coagulation/flocculation/sedimentation process, granular activated carbon filtration, and a DBP hot spot in the water distribution system. Regardless of influent water quality, photocatalysis reduced DBP precursors; however, low-energy limited photocatalysis (<5 kW h m(-3)), exacerbated the production of TTHMs and HAA5s beyond initial levels. Accordingly, limited photocatalysis is not a suitable option when 1THM5 and HAA5s are a concern, regardless of the level of pretreatment. Limited photocatalysis yields incomplete oxidation, wherein larger, more aromatic, humic organic compounds are broken into smaller molecular weight, less aromatic, and less humic moieties, which have considerable potential to produce DBPs. More complete mineralization of DBP precursors is obtained using extended photocatalysis (80-160 kW h m(-3)), which substantially decreases DBP precursors as well as TTHM and HAAS concentrations. In order to balance DBP mitigation, energy, and chemical usage, targeted use of TiO2 photocatalysis is necessary in a water treatment train (e.g., extended photocatalysis at a distribution system hot spot, where the volumetrically high energy requirements may be justifiable). (C) 2014 Elsevier Ltd. All rights reserved.

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