首页> 外文会议>AWWA water quality technology conference exposition >Temporal Behavior of Post-Filter GAC Adsorbers During THM Formation and Precursor Removal
【24h】

Temporal Behavior of Post-Filter GAC Adsorbers During THM Formation and Precursor Removal

机译:THM形成和前体去除过程中后过滤器GAC吸附剂的时间行为

获取原文

摘要

The main purpose of this work was to evaluate the temporal behavior of post filteradsorbers employing different types of granular activated carbon (GAC) media in theremoval of precursors of chlorinated organics and in the formation of disinfectionbyproducts. The experimental setup was four pilot scale adsorbers – two units withmineral GAC media (CALGON Filtrasorb 300) and another two units with vegetalGAC media (CARBOMAFRA CAG 119). The four adsorbers (F1 through F4) wereoperated in parallel, with the same empty bed contact time (EBCT) of about 20 minutes.Two of them (F1-CALGON and F2-CARBOMAFRA) were fed with filtered waterfrom a Alto da Boa Vista Water Treatment Plant (ABVWTP) which was ozonated priorto feeding, in order to observe any effects of ozonation on the different adsorbers. Theother two adsorbers (F3-CALGON and F4-CARBOMAFRA) were fed with filteredwater only. The ozonation system was composed by four column shaped contactors inseries. Each column had a hydraulic detention time of 4 minutes. Ozone dosages wereapplied in the first and second columns of the series. The total ozone dosage was in therange 0.2 through 1.0 mg O_3/L and was equally split between columns 1 and 2.Evaluations of precursor removal and disinfection byproduct formation were by meansof COT, UV-254 nm determinations and THM formation potential, respectively. Thefiltered water was from the conventional ABV WTP, whose raw water source is from ahighly eutrophic reservoir with a long detention time. COT and UV-254 values for theozonation system feed water and for adsorbers F3 and F4 were in the ranges 2.0 to 2.5mg C/L and 0.02 to 0.04 cm-1, respectively. It was observed that ozonation did notaffect significantly the COT and UV-254 values. During the first thirty days of postfilter adsorber operation, COT removal efficiencies were around 80 % for F1 and F3(with CALGON GAC media) and around 40 % for F2 and F4 (with CARBOMAFRAGAC media). With sixty days of operation, COT removal efficiencies decreased to 40% and 20%, respectively and stayed that way during eight months of operation. Themineral CAG media performed better regarding COT and UV-254 removals than thevegetal CAG media. On the other hand, no significant difference in effluent quality wasobserved regarding adsorbers with same GAC media type receiving ozonated and non-
机译:这项工作的主要目的是评估采用不同类型的颗粒活性炭(GAC)介质的后过滤吸附器在去除氯化有机物前体和形成消毒副产物中的时间行为。实验装置是四个中试规模的吸附器-两个单元使用矿物GAC介质(CALGON Filtrasorb 300),另外两个单元使用vegetalGAC介质(CARBOMAFRA CAG 119)。四个吸附器(F1至F4)并行操作,相同的空床接触时间(EBCT)约为20分钟。其中两个吸附器(F1-CALGON和F2-CARBOMAFRA)分别从Alto da Boa Vista Water进水在进料前进行臭氧处理的处理厂(ABVWTP),以观察臭氧化对不同吸附器的影响。其他两个吸附器(F3-CALGON和F4-CARBOMAFRA)仅加入过滤水。臭氧化系统由四个串联的圆柱状接触器组成。每个柱的水力滞留时间为4分钟。在该系列的第一和第二栏中应用了臭氧剂量。臭氧的总剂量在0.2至1.0 mg O_3 / L的范围内,并在第1列和第2列之间平均分配。分别通过COT,UV-254 nm测定和THM形成潜力评估前体去除和消毒副产物形成。过滤后的水来自常规的ABV WTP,其原水源来自高度富营养化的水库,滞留时间长。臭氧化系统给水以及吸附剂F3和F4的COT和UV-254值分别在2.0至2.5mg C / L和0.02至0.04 cm-1的范围内。观察到臭氧化没有显着影响COT和UV-254值。在后过滤器吸附器运行的前30天中,F1和F3(使用CALGON GAC介质)的COT去除效率约为80%,F2和F4(使用CARBOMAFRAGAC介质)的COT去除效率约为40%。手术60天后,COT去除效率分别降至40%和20%,并在手术8个月内保持这种状态。矿物CAG介质在去除COT和UV-254方面比植物CAG介质表现更好。另一方面,对于相同GAC介质类型接受臭氧处理和非臭氧处理的相同吸附器,流出物质量没有观察到显着差异。

著录项

  • 来源
  • 会议地点 Cincinnati OH(US)
  • 作者单位

    Polytechnic School of Engineering University of S?o Paulo - Brazil Polytechnic School of Engineering - University of S?o Paulo Hydraulic Sanitary Engineering Department S?o Paulo - Brazil ssffilho@usp.br;

    Polytechnic School of Engineering University of S?o Paulo - Brazil Polytechnic School of Engineering - University of S?o Paulo Hydraulic Sanitary Engineering Department S?o Paulo - Brazil ricardomendes@geasanevita.com.br;

    Polytechnic School of Engineering University of S?o Paulo - Brazil Polytechnic School of Engineering - University of S?o Paulo Hydraulic Sanitary Engineering Department S?o Paulo - Brazil cmota@sabesp.com.br;

    Polytechnic School of Engineering University of S?o Paulo - Brazil Polytechnic School of Engineering - University of S?o Paulo Hydraulic Sanitary;

  • 会议组织
  • 原文格式 PDF
  • 正文语种
  • 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