首页> 外文学位 >The use of ozonation and biological fluidized bed treatment for the control of NOM in drinking water.
【24h】

The use of ozonation and biological fluidized bed treatment for the control of NOM in drinking water.

机译:臭氧化和生物流化床处理在控制饮用水中NOM方面的应用。

获取原文
获取原文并翻译 | 示例

摘要

Bench-scale and pilot-scale studies were conducted using Huron River water taken at the Ann Arbor Water Treatment Plant. The major water quality parameters that were monitored in this study included TOC, BDOC, UV-254 absorption, THMFP, AMW distribution, humic and non humic fractions of NOM, turbidity, pH and alkalinity.; A combination of factors, including ozone dose, hydraulic retention time, and the concentration of dissolved ozone was identified, which controlled both the destruction of organic carbon and the production of low-molecular weight organic compounds and biodegradable organic matter during ozonation. The relationships between properties of THM precursors, including TOC, UV-254, humic substances, and THMFP were established and used to investigate the efficacy of the ozonation and biological fluidized bed treatment (FBT). A mathematical model that described the transformation of NOM during ozonation was developed and verified over a range of ozone doses of up to 3 mg/mg C, temperatures of up to 25°C, and hydraulic retention times of up to 20 minutes.; The biodegradable organic matter in Huron River water consisted of rapidly and slowly biodegrading fractions (“fast” and “slow” BDOC). The biodegradability of raw and treated waters was characterized by the maximum biodegradation rate of “fast” BDOC (Rmax), the minimum biodegradation time that required to eliminate “fast” BDOC (EBCTmin), and by the minimum concentration of “slow” BDOC that remained in the water after biodegradation at EBCTmin (BDOCslow).; The following treatment processes that included ozonation and FBT were investigated: (1) single-pass ozonation/FBT; (2) ozonation/FBT with recycle; (3) single-pass FBT/ozonation with biofiltration; (4) recirculating FBT/ozonation with biofiltration; (5) single-pass FBT/ozonation/biofiltration with the addition of acetate to the FBT column (“stimulated” FBT); and (6) recirculating “stimulated” FBT/ozonation with biofiltration. Among these processes, the recirculating “stimulated” FBT/ozonation process followed by biofiltration was most efficient in terms of the removal of NOM relative to ozone consumption and biodegradation time. The removal of NOM was comparable to that achieved at the Ann Arbor Water Treatment Plant, that uses lime softening, flocculation/sedimentation, ozonation and GAC filtration. For a design capacity of 1 MGD, the cost of treatment by the FBT/ozonation process followed by biofiltration was estimated to be at least 40 percent lower than that by a conventional flocculation/sedimentation process with ozonation and GAC filtration.
机译:使用在安阿伯水处理厂获得的休伦河水进行基准规模和中试规模的研究。这项研究中监测的主要水质参数包括TOC,BDOC,UV-254吸收,THMFP,AMW分布,NOM的有毒和无毒成分,浊度,pH和碱度。确定了包括臭氧剂量,水力停留时间和溶解的臭氧浓度在内的多种因素,这些因素既控制了有机碳的破坏,又控制了臭氧化过程中低分子量有机化合物和可生物降解有机物的产生。建立了THM前体(包括TOC,UV-254,腐殖质和THMFP)的性能之间的关系,并用于研究臭氧化和生物流化床处理(FBT)的功效。建立了描述臭氧氧化过程中NOM转化的数学模型,并在高达3 mg / mg C的臭氧剂量,高达25°C的温度和长达20分钟的水力停留时间的范围内进行了验证。休伦河水中的可生物降解有机物包括快速和缓慢的生物降解级分(“快速”和“慢速” BDOC)。原水和处理后水的生物降解性的特征在于“快速” BDOC的最大生物降解率(R max ),消除“快速” BDOC所需的最小生物降解时间(EBCT min < / sub>),以及在EBCT min (BDOC slow )生物降解后残留在水中的“慢” BDOC的最低浓度。研究了以下处理过程,包括臭氧化和FBT:(1)单次臭氧化/ FBT; (2)带再生的臭氧化/ FBT; (3)具有生物过滤的单程FBT /臭氧化; (4)通过生物滤池再循环FBT /臭氧化; (5)在FBT柱中添加乙酸盐的单程FBT /臭氧化/生物滤池(“受激” FBT); (6)通过生物过滤循环“刺激”的FBT /臭氧化。在这些过程中,就去除NOM而言,相对于臭氧消耗和生物降解时间而言,循环“刺激”的FBT /臭氧化过程随后进行生物过滤是最有效的。 NOM的去除与使用石灰软化,絮凝/沉淀,臭氧化和GAC过滤的安阿伯水处理厂的去除率相当。对于设计容量为1 MGD的设备,通过FBT /臭氧化工艺再进行生物过滤的处理成本估计比采用臭氧化和GAC过滤的常规絮凝/沉淀工艺的成本至少低40%。

著录项

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