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A case study on the automatic ozone dose control system based on the ozone decay rate in a full-scale advanced water treatment plant

机译:大型先进水处理厂中基于臭氧衰减率的自动臭氧剂量控制系统的案例研究

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摘要

Recently, a growing concern about algae-origin taste and odor in drinking water made it possible to introduce ozone and granular activated carbon (GAC) processes to large-capacity (more than 300,000 m~3/d) water treatment plants in the Han River area in South Korea. Especially, concerning the ozone process, the ozone residual of ozone contactor effluent may affect on the biological desta-bilization, poor physical properties of the following GAC process and operators' health due to high ozone gas concentration in GAC contactor. Therefore, maintaining an optimal ozone dose based on the ozone demand is essential to the operation of the ozone process. The Koyang Advanced Water Treatment Plant (KAWTP) has been utilizing a new type of ozone control method since July 2009, which automatically calculates required ozone dosed based on the instantaneous ozone demand (ID) and the ozone decay rate constant (K_c). The ID and the first-order K_c values are calculated based on the measured dissolved-ozone concentrations from at least three points of ozone contactor. After the calculations of ID and K_c values, the values were applied for the proportional integral derivative (PID) ozone dose control system. PID control is operated through two different methods. The first involves automatic controlling the ozone dose, by which the ozone residual of the effluent from the ozone contactor will be maintained at the desired value set by the operator. The second method was the modified extended CSTR method, which was appropriately modified to fit the KAWTP site specifications, to calculate the Cryptosporidium, Giardia and virus log inactivation automatically. An automatic ozone dose control system based on the ozone decay rate overcomes the disadvantages of the previous ozone control systems, including late response and variation of effluent ozone residual. In the earlier pilot scale research, an extra device for measuring K_c and ID was used. In this study, the ozone dose was determined by measuring K_c in the full-scale ozone process. It is the first case in Korea that applied ID-K,-based ozone dose control to a full-scale water treatment plant. According to the operation results of the automatic ozone dose control system based on K_c calculation, adequate-ozone-dose calculation along with the various water quality and inflow rate was performed successfully, and the ozone residual of the effluent was also maintained below the lowest set value during operation. Moreover, the process was adequately run to maintain the target log inactivation the Cryptosporidium. Also, calculating the optimal ozone dose that could completely oxidize ozone-consuming matters and leave minimum residual, could be economical due to excessive ozone dose saving, and the biological and physical stability of GAC granule in GAC process.
机译:最近,人们越来越关注饮用水中藻类的味道和气味,这使得有可能将臭氧和颗粒状活性炭(GAC)工艺引入汉江的大容量(300,000 m〜3 / d)以上的水处理厂韩国地区。特别是在臭氧处理方面,由于GAC接触器中的高浓度臭氧气体,臭氧接触器流出物中的臭氧残留可能会影响生物稳定性,后续GAC过程的较差物理性能以及操作人员的健康。因此,基于臭氧需求维持最佳臭氧剂量对于臭氧工艺的操作至关重要。自2009年7月起,高阳市高级水处理厂(KAWTP)就开始使用一种新型的臭氧控制方法,该方法根据瞬时臭氧需求量(ID)和臭氧衰减速率常数(K_c)自动计算所需的臭氧剂量。 ID和一阶K_c值是根据从臭氧接触器的至少三个点测得的溶解臭氧浓度计算得出的。在计算完ID和K_c值之后,将这些值应用于比例积分微分(PID)臭氧剂量控制系统。 PID控制通过两种不同的方法进行操作。第一个涉及自动控制臭氧剂量,通过该剂量,臭氧接触器流出物的臭氧残留量将保持在操作员设定的期望值。第二种方法是修改后的扩展CSTR方法,该方法经过适当修改以适合KAWTP站点规范,以自动计算隐孢子虫,贾第鞭毛虫和病毒日志失活。基于臭氧衰减率的自动臭氧剂量控制系统克服了以前的臭氧控制系统的缺点,包括反应迟钝和废水中残留臭氧的变化。在较早的中试规模研究中,使用了额外的设备来测量K_c和ID。在这项研究中,臭氧剂量是通过在满量程臭氧过程中测量K_c来确定的。这是韩国首例将基于ID-K的臭氧剂量控制应用于大规模水处理厂的案例。根据基于K_c计算的自动臭氧剂量控制系统的运行结果,成功进行了适当的臭氧剂量计算以及各种水质和入水率,并且废水中的臭氧残留量也保持在最低设置以下操作期间的价值。此外,该过程已充分运行以维持目标对数灭活了隐孢子虫。同样,计算最佳的臭氧剂量可以完全氧化消耗臭氧的物质,并留下最少的残留物,由于节省了过多的臭氧剂量以及GAC流程中GAC颗粒的生物和物理稳定性,可能是经济的。

著录项

  • 来源
    《Desalination and water treatment》 |2011年第3期|p.337-350|共14页
  • 作者单位

    Korea Water Resources Corporation, San 6-1 Yonchook-dong, Deadeok-gu, Deajeon-si 306-711, Korea,Department of Civil & Environmental Engineering, College of Engineering, Yonsei University, Seoul 120-749, Korea;

    Korea Water Resources Corporation, San 6-1 Yonchook-dong, Deadeok-gu, Deajeon-si 306-711, Korea;

    Korea Water Resources Corporation, San 6-1 Yonchook-dong, Deadeok-gu, Deajeon-si 306-711, Korea;

    Korea Water Resources Corporation, San 6-1 Yonchook-dong, Deadeok-gu, Deajeon-si 306-711, Korea;

    Korea Institute of Construction Technology, 2311 Deahwa-dong, Rsan-gu, Goyang-si, Kyonggi-do 411-712, Korea,Department of Civil & Environmental Engineering, College of Engineering, Yonsei University, Seoul 120-749, Korea;

    Department of Civil & Environmental Engineering, College of Engineering, Yonsei University, Seoul 120-749, Korea;

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

    ozone; automatic control; ID (instantaneous ozone demand); K_c (ozone decay rate constant); full-scale;

    机译:臭氧;自动控制;ID(瞬时臭氧需求);K_c(臭氧衰减率常数);全尺寸;

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