期刊文献+

Evaluating the effects of granular and membrane filtrations on chlorine demand in drinking water 被引量:1

Evaluating the effects of granular and membrane filtrations on chlorine demand in drinking water
下载PDF
导出
摘要 In this study, chlorine decay experiments were conducted for the raw water from Nakdong River that is treated by Chllseo Water Treatment Plant (CWTP) situated in Haman, Korea as well as the effluents from sand and granular activated carbon (GAC) filters of CWTP and fitted using a chlorine decay model. The model estimated the fast and slow reacting nitrogenous as well as organic/inorganic compounds that were present in the water. It was found that the chlorine demand due to fast and slow reacting (FRA and SRA) organic/inorganic substances was not reduced significantly by sand as well as GAC filters. However, the treated effluents from those filters contained FRA and SRA that are less reactive and had small reaction rate constants. For the effluents from microfiltration, ultrafiltration, and nanofiltration the chlorine demand because FRA and SRA were further reduced but the reaction rate constants were larger compared to those of sand and GAC filter effluents. This has implications in the formation of disinfection by products (DBPs). If DBPs are assumed to form due to the interactions between chlorine and SRA, then it is possible that the DBP formation potential in the effluents from membrane filtrations could be higher than that in the effluents from granular media filters. In this study, chlorine decay experiments were conducted for the raw water from Nakdong River that is treated by Chllseo Water Treatment Plant (CWTP) situated in Haman, Korea as well as the effluents from sand and granular activated carbon (GAC) filters of CWTP and fitted using a chlorine decay model. The model estimated the fast and slow reacting nitrogenous as well as organic/inorganic compounds that were present in the water. It was found that the chlorine demand due to fast and slow reacting (FRA and SRA) organic/inorganic substances was not reduced significantly by sand as well as GAC filters. However, the treated effluents from those filters contained FRA and SRA that are less reactive and had small reaction rate constants. For the effluents from microfiltration, ultrafiltration, and nanofiltration the chlorine demand because FRA and SRA were further reduced but the reaction rate constants were larger compared to those of sand and GAC filter effluents. This has implications in the formation of disinfection by products (DBPs). If DBPs are assumed to form due to the interactions between chlorine and SRA, then it is possible that the DBP formation potential in the effluents from membrane filtrations could be higher than that in the effluents from granular media filters.
出处 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2009年第1期23-29,共7页 环境科学学报(英文版)
基金 supported by Kyungnam University, Masan, Korea.
关键词 chlorine decay model initial concentration nitrogenous compounds organic and inorganic compounds reaction rate constants chlorine decay model initial concentration nitrogenous compounds organic and inorganic compounds reaction rate constants
  • 相关文献

参考文献15

  • 1APHA (American Public Health Association), 1998. Standard Methods for the Examination of Water and Wastewater (19th ed.). Washington DC, USA.
  • 2Biswas P, Lu C, Clark R M, 1993. A model for chlorine concentration decay in pipes. Water Research, 27(12): 1715-1724.
  • 3Boccelli D L, Tryby M E, Uber J G, Summers R S, 2003. A reactive species model for chlorine decay and THM formation under re-chlorination conditions. Water Research, 37(11): 2654-2666.
  • 4Bolto B, Braun G B, Dixon D, Eldrige R, Frimmel F, Hesse S, King S, Toifl M, 1999. Experimental evaluation of cationic polyelectrolyte for removing natural organic mater from water. Water Science and Technology, 40(9): 71-80.
  • 5Butterfield P W, Camper A K, Ellis B D, Jones W L, 2002. Chlorination of model drinking water biofilm: implications for growth and organic carbon removal. Water Research, 36(17): 4391--4405.
  • 6Chow C W K, Fabris R, Dfikas M, 2004. A rapid fractionation technique to characterize natural organic matter for the optimization of water treatment processes. Journal of Water Supply: Research and Technology, 53(2): 85-92.
  • 7Clark M R, 1998. Chlorine demand and TTHM formation kinetics: A second order model. Journal of Environmental Engineering, 124(1): 16-24.
  • 8Eikebrokk B, Julma T, Osterhus S W, 2006. Water treatment by enhanced coagulation - Operational status and optimization issues. TECHNEAU, Deliverable Number D 5.3.1.A.
  • 9Jegatheesan V, Kastl G, Fisher I, Chandy J, Angles M, 2004. Modelling bacterial growth in drinking water: effect of nutrients. Journal of AWWA, 96(5): 129-141.
  • 10Jegatheesan V, Shu L, Streeter M, Fracchia H, 2003. Efficient management of drinking water distribution systems through the application of water quality modeling. In: Proceedings of ASIAN WATERQUAL 2003. IWA Asia-Pacific Regional Conference. Oct. 19-23, Bangkok.

同被引文献5

引证文献1

二级引证文献3

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部