期刊文献+

压力协同渗透和反渗透联合处理再生水特性研究

Study on the Effect of Pressure on PAO and the Characteristics of the Joint Treatment of Reclaimed Water with RO
下载PDF
导出
摘要 分别研究了压力协同渗透(PAO)和反渗透(RO)运行过程,在此基础上分析了PAO—RO组合工艺处理再生水的特性,并采用凝胶色谱分析了处理过程中相对分子质量的分布变化情况。结果表明,正渗透(FO)膜结构性能测试过程中,使用网格垫片时,FO膜的纯水渗透系数A和盐渗透系数B均有增加,且随着压力增加而增加。在单一PAO过程中,纯水通量与压力成正相关,盐返混通量成下降趋势。以二沉出水为原料液,海水为汲取液,采用PAO—RO联合工艺,运行12h后,系统产水量较单独RO工艺增加约150%,海水脱盐率达到94.8%,对二沉出水TOC的去除率达到99%以上,出水相对分子质量主要分布在80-500。 In this study, the operating process of pressure assited osmosis (PAO) and reverse osmosis (RO) were studied, and on this basis, the characteristics of reclaimed water processed by PAO-RO combination process was analyzed, and the molecular weight distribution was also analyzed using gel permeation chromatography. The results showed that: the pure water permeability coefficient A and salt permeability coefficient B of FO membrane were both increased with the increase of pressure, during the test of performance of the membrane structure while using spacer support. In a single PAO process, Jw was positively related to the pressure, and the J~ was decreased. When the secondary effluent was feed solution, and seawater was draw solution, the combined process of PAO-RO was used. After the process run 12 h, the water production capacity of the system increase by about 150% than single RO process, and the seawater desalination rate, TOC of secondary effluent water removal rate reached to 94.8%, more than 99% respectively, and relative molecular mass of effluent was mainly distributed ranged from 80-500.
出处 《水处理技术》 CAS CSCD 北大核心 2016年第11期78-82,88,共6页 Technology of Water Treatment
基金 国家自然科学基金资助项目(21477018 21007010) 交通运输部科技项目(2010353343290) 中央高校基本科研业务费专项资金重点项目(15D111323)
关键词 压力协同渗透 再生水 反渗透 海水 pressure assited osmosis reclaimed water reverse osmosis seawater
  • 相关文献

参考文献24

  • 1Butler E, Silva A, Horton K, et al. Point of use water treatment with forward osmosis for emergency relief[J].Desalination,2013,312(3): 23-30.
  • 2Kerusha L, Comelissen E R, Harmsen D J H, et al. Water recovery from sewage using forward osmosis[J].Water Science & Technology A Journal of the International Association on Water Pollution Research, 2011,64(7): 1443 -9.
  • 3Su J, Zhang S, Ling M M, et al. Forward osmosis: an emerging tech- nology for sustainable supply of clean water[J].Clean Technologies & Environmental Policy,2012,14(4):507-511.
  • 4Nasr P, Sewilam H. Forward osmosis: an alternative sustainable technology and potential applications in water industry[J].Clean Technologies & Environmental Policy,2015,17(7): 1-12.
  • 5Cath T Y, Drewes J E, Lundin C D, et al. Forward osmosis-reverse osmosis process offers a novel hybrid solution for water purification and reuse [J].Maney Publishingsuitec Josephs Well Hanover Walk Leeds Ls3ab Uk,2010,2(4): 16-20.
  • 6Bamaga O A, Yokochi A, Zabara B, et al. Hybrid FO/RO desalination sysmu: Preliminary assessauent of osmotic energy recovery and designs of new FO membrane module configurations [J].Desalination,2011, 268(1/3):163-169.
  • 7Cath T Y, Hancock N T, Lundin C D, et al. A multi-barrier osmotic dilution process for simultaneous desalination and purification of impaired water[J].Journal of Membrane Science,2010,362(S1/2): 417-426.
  • 8Blandin G, Le-Clech A V P. Pressure-assisted osmosis (PAO)-RO hybrid: impact of hydraulic pressure on fouling and economics[J]. Desalination & Water Treatment,2015,55(11):3-160-3161.
  • 9Achilli A, Childress A E, Cath T Y. Power generation with pressure retarded osmosis: An experimental and theoretical investigation[J]. Journal of Membrane Science,2009,343(1/2):42-52.
  • 10Tang C Y, She Q, Lay W C L, et al. Coupled effects of internal concentration polarization and fouling on flux behavior of forward osmosis membranes during humic acid filtration[J].Journal of Membrane Science,2010,354( 1 ): 123-133.

二级参考文献35

  • 1王磊,刘莹,王旭东,段文松,韩勤有.用膜结构参数模型评价溶解性有机物分子量分布对超滤膜污染的影响研究[J].环境工程,2005,23(6):81-83. 被引量:5
  • 2王磊,王旭东,刘莹,段文松.臭氧预氧化对城市二级处理水中残留有机物分子量分布的影响及超滤膜阻力变化分析[J].膜科学与技术,2006,26(2):27-31. 被引量:14
  • 3王磊,福士ほか.河川水に对象とした限外も过とろ过による膜ろ过验[C].第49回全国水道研究会讲演概要集,1998,188-189.
  • 4James A nilson, Francis A Digino. Influence of NOM composition on nanofiltration[J]. AWWA, 1996,88 (5):53-56.
  • 5Wang L, Fukuslai K, Sato A. A fundamental study on the application ofnanofiltration to water treatment [J]. Japan Water Works Association ,2000,69 (5) :35-45.
  • 6Aiken G, Cotsaris E. Soil and Hydrology : their effect on NOM[J]. JAWWA ,1995, (1):35-45.
  • 7Widrig D L, Gray K A, Mcauliffe K S. Removal of algal derived organic material by preozonation and coagulation :monitoring changes of organic quality by pyrolysis CJC MS [J].Wat Res., 1996, 30 (11) 2621-2632.
  • 8Chiou C T, Malcolm R L, Brinton T I, et al . Water solubility enhancement of some organic pollutants and pesticides by dis solved humie and fulvic acids [J].Envir Sci Teehnol.,1986,20(5): 502-508.
  • 9Cath T Y, Childress A E, Elimelech IV[ Forward os- mosis: Principles, applications, and recent develop- ments[J]. J Membr Sci, 2006, 281(1): 70-87.
  • 10Chung T, Zhang S, Wang K Y, etal. Forward osmosis processes: yesterday, today and tomorrow[J]. Desali- nation. 2012, 287: 78-81.

共引文献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