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The effect of loading rate on tertiary wastewater filtration.

机译:加载速率对第三级废水过滤的影响。

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his study aimed to improve our scientific understanding of the role filter loading rate plays in filtration performance, through pilot-scale filter testing, followed by full-scale filter testing at several California water recycling plants, while also examining how coagulation and particle association affect virus removal through filtration.;The impact of loading rate on tertiary filtration of wastewater was studied using a pilot-scale, dual-media (sand and anthracite), rapid-depth filtration system. Loading rates of 5, 6.25, 7.5, 8.75, and 10.0 gal/ft2-min (12.2, 15.3, 18.3, 21.4, and 24.4 m/h) were tested on parallel filter columns treating the same coagulated secondary wastewater to determine the impact on removal of turbidity, particles (2-15 mum), total coliform bacteria, E. coli, and seeded MS2 bacteriophage, as well as on the particle deposition profile in the filter bed. For all conditions studied, loading rate had no observable impact on the ability to disinfect filter effluents with chloramines. The results of the pilot-study provided support and justification for testing loading rates higher than 5 gal/ft2-min at full-scale water recycling facilities in California.;Full-scale granular media filter studies comparing loading rates of 12.2 and 18.3 m/h (5.0 and 7.5 gal/ft2-min) were conducted at water recycling facilities in Monterey County and San Jose, CA. At the Monterey plant, 51% more coagulant was required at the higher loading rate to achieve equivalent 5-15 mum particle counts in the effluent (no difference between rates); with this coagulant dose the effluent turbidity and 2-5 mum particles were significantly lower at the higher loading rate (22 and 19%, respectively). At the San Jose plant, where no coagulant was added, increasing the loading rate from 12.2 to 18.3 m/h had minimal impact on the filter effluent quality (5.4, 3.1, and 11% increases for turbidity, 2-5 and 5-15 mum particles, respectively while operating at 18.3 m/h). No decrease in the ability to disinfect the filter effluent was observed at either plant.;The effect of coagulation on virus-particle association and removal of viruses through filtration was studied using three bacteriophages with varying isoelectric points. MS2, PRD1, and phiA174 bacteriophages were co-seeded into bench-scale jar tests and different coagulant types (aluminum chlorohydrate (ACH) and two different cationic polymers) and doses (0-100 mg/L) were applied. When properly coagulated, MS2 and PRD1 were associated with positively charged coagulant precipitates, which in turn were strongly attracted to the negatively charged filter media. In the absence of coagulant, the negatively-charged unassociated viruses still exhibited forces repulsive to the filter media as it passed through the filter. This is the first study to show that removal of viruses through tertiary wastewater filters was a result of association with particles formed during coagulation.;The results from this study have significant implications for California water recycling regulations and water reuse economics. Based on the findings, the Monterey Regional Water Pollution Control Agency was granted a permanent waiver from the 5 gal/ft2-min limit and are now able to operate water recycling filters at 7.5 gal/ft2-min, which has expanded plant capacity by 50% and saved approximately
机译:他的研究旨在通过中试规模的过滤器测试,然后在加利福尼亚的几家水循环厂进行全面的过滤器测试,来提高我们对过滤器负载率在过滤性能中所起的作用的科学理解,同时还研究凝结和颗粒缔合如何影响病毒使用中试规模,双介质(砂和无烟煤),快速深度过滤系统研究了负载量对废水三次过滤的影响。在平行过滤器柱上测试了5、6.25、7.5、8.75和10.0 gal / ft2-min(12.2、15.3、18.3、21.4和24.4 m / h)的加载速率,以确定对第二次凝结后的废水的影响去除浊度,颗粒(2-15微米),大肠菌,大肠杆菌和种子MS2噬菌体,以及滤床中的颗粒沉积情况。在所研究的所有条件下,加料速率对用氯胺消毒过滤器废水的能力均未观察到影响。该试点研究的结果为在加利福尼亚州的全尺寸水回收设施中测试高于5 gal / ft2-min的加载速率提供了依据和依据。;大型颗粒介质过滤器研究比较了12.2和18.3 m / h(5.0和7.5 gal / ft2-min)在加利福尼亚州蒙特雷县和圣何塞的水循环设施进行。在蒙特雷工厂,以较高的上样速度需要更多的凝结剂才能达到废水中等效的5-15微米颗粒计数(速率之间无差异)。在此凝结剂剂量下,较高的负载率(分别为22%和19%)时,出水浊度和2-5毫米颗粒明显降低。在不添加凝结剂的圣何塞工厂中,将装填速率从12.2 m / h提高到18.3 m / h对滤池出水质量的影响最小(浊度分别提高5.4、3.1和11%,2-5和5-15)颗粒,分别以18.3 m / h的速度运行)。在任何一家工厂中,都没有观察到对过滤器出水进行消毒的能力的下降。使用三种等电点不同的噬菌体研究了混凝对病毒-颗粒缔合和通过过滤去除病毒的影响。将MS2,PRD1和phiA174噬菌体共同接种到实验室规模的广口瓶试验中,并应用不同的混凝剂类型(水合氯化铝(ACH)和两种不同的阳离子聚合物)和剂量(0-100 mg / L)。正确凝结后,MS2和PRD1与带正电的凝结剂沉淀物相关联,而这些沉淀物又被强烈吸引到带负电的过滤介质中。在不存在凝结剂的情况下,带负电荷的未缔合病毒在通过过滤器时仍表现出排斥力。这是第一项表明通过三级废水过滤器去除病毒是与凝结过程中形成的颗粒相关联的结果。该研究的结果对加利福尼亚州的水循环法规和水回用经济学具有重大意义。根据调查结果,蒙特雷区域水污染控制局被永久性豁免5加仑/分钟2分钟的限制,现在能够以7.5加仑/平方英尺2分钟的速度运行水循环过滤器,这使工厂的产能增加了50倍%,大约节省了

著录项

  • 作者

    Williams, Gordon Johnson.;

  • 作者单位

    University of California, Berkeley.;

  • 授予单位 University of California, Berkeley.;
  • 学科 Water Resource Management.;Environmental Sciences.;Engineering Environmental.
  • 学位 Ph.D.
  • 年度 2009
  • 页码 250 p.
  • 总页数 250
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

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