期刊文献+

连续式泡沫分离器深度处理胶团强化超滤渗透液中的SDS和Cd^(2+) 被引量:2

Surfactant SDS and Cd^(2+) recovery from permeate in MEUF using a continuous foam fractionator
下载PDF
导出
摘要 利用泡沫分离技术,对胶团强化超滤(MEUF)工艺处理含SDS和Cd2+所得渗透液中SDS的回收进行了研究,考察了影响表面活性剂SDS(十二烷基硫酸钠)和金属Cd2+去除率,富集率及夹带率的操作参数(空气流速?泡沫高度?液面高度),溶液体系性质(表面活性剂SDS进料浓度、pH值、离子强度和乙醇的添加量)等因素对分离效果的影响.实验结果表明,当胶团强化超滤废水中初始SDS和Cd2+的浓度为1440mg·L-1和50mg·L-1时,排出的渗透液中含SDS和Cd2+浓度分别为500mg·L-1和10mg·L-1,在最佳的工艺条件下(曝气头孔径为10μm,空气流速为100L·h-1,液体流速为5L·h-1,泡沫高度为66cm,液面高度为45cm),SDS和Cd2+的去除率分别达52%和99.35%,SDS富集比为3.1.Cd2+出水浓度低于0.1mg·L-1,达到GB8978-1996国家污水排放标准. The purpose of this study was to investigate the use of foam fractionation to recover surfactant SDS and Cd^2+ from micenar-enhanced ultrafiltration (MEUF) permeate. The effects of air flow rate,liquid-and vapor-phase heights ,liquid feed surfactant concentration, solution pH, suspension ionic strength, and concentration of ethanol on separation characteristics were studied in continuous operation. The results showed that when the concentration of surfactant (SDS) and metal ions ( Cd^2+ ) in the feed solution were 500 m·L^ -1 and 10 m·L^ -1, optimum conditions were air and liquid flow rates 100 L·h^- 1 and 5L·h^- 1, liquid- and vapor- phase heights 45 cm and 66 cm,respectively,sparger (pore size 10 μm). Under the optimum conditions,the about 52% SDS and 99.35% Cd^2+ were removed. The enrichment ratio of SDS was 3.1 and Cd^2+ in the effluent was less than 0. 1 mg·L^-1 ,which meets the top grade national discharge standard.
出处 《环境科学学报》 CAS CSCD 北大核心 2007年第8期1256-1262,共7页 Acta Scientiae Circumstantiae
基金 国家重点基础研究计划(973)项目(No.2005CB724203) 国家自然科学基金(No.50608028) 湖南省教育厅资助科研项目([2005]100)~~
关键词 泡沫分离法 胶团强化超滤 表面活性剂SDS 金属离子Cd2+ foam fractionation micellar-enhanced ultrafiltration (MEUF) surfactant(SDS) metal ions (Cd^2+)
  • 相关文献

参考文献17

  • 1Akay G,Wakeman R J.1994.Ultrafiltration and microfitration of surfactant dispersions-An evaluation of published research[ J ].Sep Sci and Tech,29 (18):411-420.
  • 2Chrastopher E L,Paul M B,Michael J.1997.Purification of Proteins Using Foam Fractionation[ J ].Pharmaceutical Research,14(11):1511-1515.
  • 3Chung C T,Yu M Y.2002.Removal of copper ions and dissolved phenol from water using micellar enhanced ultrafiltration with mixed surfactants[J].Water Management,22:695-701.
  • 4Krit K,John F S.1999.Surfactant Recovery from Water Using Foam Fractionation:Effect of Temperature and Added Salt[ J].Sep Sci and Tech,34 (2):157-172.
  • 5Liu M E,Chen H L.1993.New separate technique foundation[ M].Hangzhou:Zhejiang University Press,18-65 .
  • 6Liu Z H,Liu Z,Ding F X.1997.Concentration and separation of proteins by foam fractionationI[ J ].Journal of Tsinghua University,37 (12):50-54.
  • 7Nopparat,John F S.1996.Surfactant Recover from Water Using Foam Fractionation[J].Sep Sci and Tech,31 (9):1233-1258.
  • 8Okamoto Y,Chou E J.1976.Removal of cadmium ion from aqueous solution[J].J Water Poll Control Fed,48 (2):2747-2753.
  • 9Pukpong W,John F S,Sumaeth C.1996.Use of Foam Flotation to Remove Tert-butylphenol from Water[ J ].Sep Sci Tech,31(11):1523-1540.
  • 10Savanit B,Sumaeth C,Pomthong M.2003.Anionic and cationic surfactant recovery from water using a multistage foam fractionator[ J].Chemical Engineering Journal,93:241-252.

同被引文献42

引证文献2

二级引证文献1

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