期刊文献+

大孔强碱阴树脂去除饮用水中微量有机物 被引量:4

Removing Trace Organic Substances from Drinking Water by Macro Porous Strong Base Anion Resin
在线阅读 下载PDF
导出
摘要 比较了大孔强碱阴树脂和颗粒活性炭在饮用水的深度处理中对有机物的去除效果。结果表明:(1)大孔强碱阴树脂的吸附容量比颗粒活性炭的大。在pH为8时,大孔强碱阴树脂对TOC的去除率最高,pH6~8时,对TOC的去除率没有明显的区别,而颗粒活性炭在pH为2时,对TOC的去除率最高;水温低能提高2种吸附材料的吸附容量。(2)在动态实验条件下,当流速相同,大孔强碱阴树脂的穿透时间明显比颗粒活性炭的长,大孔强碱阴树脂的制水量约是吸附床的10000倍,而颗粒活性炭却只有吸附床的4000倍。在饮用水的深度处理中,大孔强碱阴树脂可作为活性炭的最佳替代品。 Comparative study on adsorption characteristics of trace organic substances in deep treatment of drinking water between macro porous strong base anion resin and granular activated carbon (GAC) has been con-ducted. The result showed that the adsorption capac ity of macro porous strong base anion resin was far greater than that of GAC. The highest removal effect of TOC on macro porous strong base anion resin and GAC was at pH 8 and pH 2 respectively, but there was no distinct difference at pH6 - 8 for macro porous strong base anion resin. At lower temperature it in-creased adsorbing capacity of resin and GAC. In dy-namic experiments, when flow rate was same, the breakthrough time of resin was much longer than that of GAC, and the amount of produced water was about 10000 times but GAC only 4000 times than the adsorption bed volumes. So the resin could be used to substitute GAC in deep treatment of drinking water.
出处 《上海环境科学》 CAS CSSCI CSCD 北大核心 2003年第9期609-614,共6页 Shanghai Environmental Sciences
关键词 大孔强碱阴树脂 饮用水 有机物 活性炭 TOC 吸附容量 制水量 腐殖质 Deep treatment of drinking water Macro porous strong base anion resin GAC Trace organic pollutants Removal of TOC
  • 相关文献

参考文献10

  • 1张燕,王志奇,陈英旭.微污染水源水的控制技术[J].环境污染与防治,2001,23(2):69-71. 被引量:39
  • 2杨靖,周柏青,钱达中,黄荣华,李芹.饮水有机物污染的控制[J].水处理技术,2001,27(3):125-128. 被引量:25
  • 3U S Environmental Protection Agency. Treatment techniques for controlling trihalomethanes in drink-ing water. EPA/600/2-81/156. Washington, D C:USEPA, 1981.
  • 4Chen P H, Jenq C H, wang Y J. Using adsorbents to remove trace organic in drinking water. J Soil Water Conservation Taiwan, R O C 1994,26(2):1-15.
  • 5Najm I N,Snoeyink V L, Suidan M T, et al.Effect of particle size and background natural organics on the adsorption efficiency of PAC J AWWA, 1990,82:65-72.
  • 6Malcolm R L, MacCarthy P. Quantitative evaluation of XAD-8 and XAD-4 resins used intandem for removing organic solutes from. Environ lnt, 1992,18:597 - 607.
  • 7GOTO M, Hayashi N, GOTO S. Adsorption and desorption of phenol on anion exchange resins and activated carbon. Environ. Sci. Technol, 1986,20:463 - 467.
  • 8Joachim Fettig. Removal of humic substances by adsorption/ion exchange. Wat Sci Tech , 1999,40(9): 173- 182.
  • 9Chen, P H, Jenq, C H, Chen K M. Evaluation of granular activated carbon for removal of trace organic compounds in drinking water. Environ Int , 1996,22(3 ):343 - 359.
  • 10Fu P L K, Symons J M. Removing aquatic organic substances by anion exchange resins. J AWWA, 1990,82:70-77.

二级参考文献20

共引文献60

同被引文献55

引证文献4

二级引证文献7

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