期刊文献+

纯水体系下纳滤膜分离过程热力学问题研究 被引量:2

Thermodynamics study of the separation process of nanofiltration membrane in pure water system
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摘要 采用NF270和GE DK纳滤膜,在不同压力、温度和pH条件进行纯水过滤试验,以测定不同条件下两种纳滤膜的膜通量,并研究不同条件下的纳滤膜渗透系数变化规律;构建纳滤膜渗透系数与热力学参数之间的关系式,计算两种纳滤膜的热力学参数,分析两种纳滤膜分离过程热力学原理.结果表明:两种纳滤膜的膜通量随着温度和压力的增加而增大,两种纳滤膜的渗透系数随着温度升高而增大,并随着压力和pH的变化呈现小幅波动;GE DK纳滤膜的活化能高于NF 270纳滤膜的活化能,分别为16.56kJ/mol和14.22kJ/mol.由此可知,在分离过程中GE DK纳滤膜比NF 270纳滤膜需更高的运行压力. Two nanofiltration(NF)membranes,NF 270 and GE DK,were tested for the filtration process in pure water system at different temperatures,operating pressures and pH for water.The fluxes of the two NF membranes were determined,and the variations of pure water permeability coefficient of NF membranes were discussed.The relationship between pure water permeability coefficient of NF membranes and thermodynamic parameters were conducted and the thermodynamic parameters of the two types of NF membranes were calculated.Following that,the principle of the filtration process of NF membrane was discussed.The experimental results show that the fluxes of the two NF membranes increased with increasing the temperature and operating pressure.The pure water permeability coefficient of both NF membranes also increased with increasing the temperature and fluctuated within a narrow range with the change of operating pressure and pH for water.The activation energy of GE DK membrane is higher than that of NF 270 membrane,16.56kJ/mol and 14.22kJ/mol,respectively.This indicates that GE DK membrane requires more energy to run than NF 270 membrane.
出处 《膜科学与技术》 CAS CSCD 北大核心 2014年第5期79-83,共5页 Membrane Science and Technology
基金 科技部 财政部国家中小企业创新基金 武汉大学博士创新基金的资助
关键词 纳滤膜 热力学 纯水体系 NF membrane thermodynamics pure water system
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参考文献8

  • 1Ventresque C., Gisclon V., Bablon G., et al, An outstanding feat of modem technology: the Méry-sur-Oise nanofiltration treatment plant (340,000m3/d) [J], Desalination, 131 (2000): l-16. 被引量:1
  • 2牟旭凤,白庆中,陈红盛,李维臻.聚合物辅助超滤/纳滤技术处理模拟放射性废水[J].给水排水,2006,32(z1):174-177. 被引量:10
  • 3李晓明,王铎,柴涛,苏保卫,高高堦.纳滤海水软化的实验研究[J].高校化学工程学报,2009,23(4):582-586. 被引量:17
  • 4王晓琳,丁宁编著..反渗透和纳滤技术与应用[M].北京:化学工业出版社,2005:400.
  • 5Saitua H., Gil R., Perez Padilla A., Experimental investigation on arsenic removal with a nanofiltration pilot plant fromnaturally contaminated groundwater [J], Desalination, 274 (2011):1-6. 被引量:1
  • 6Van der Bruggen B., Hawrijk I., Cornelissen E., et al, Direct nanofiltration of surface water using capillary membranes: comparison with flat sheet membranes[J], Separation and Purification Technology, 31(2003):193-200. 被引量:1
  • 7Tsuru, T., Izumi, S., Yoshiaoka, T. and Asaeda, M., Temperature effect on transport performances by inorganic nanofiltration membranes[J], AIChE Journal, 46 (2000): 565-574. 被引量:1
  • 8Zwolinski, B.J., Eyring, H., and Resse, C.E., Diffusion and membrane permeability, I[J], Journal of physical chemistry, 1949. 53: 1426-1453. 被引量:1

二级参考文献19

  • 1俞三传,高从堦,张慧.纳滤膜技术和微污染水处理[J].水处理技术,2005,31(9):6-9. 被引量:48
  • 2薛罡,刘亚男,何圣兵.纳滤膜处理受污染地下水的运行影响因素研究[J].中国给水排水,2006,22(3):24-27. 被引量:5
  • 3Hilal N, A1-Zoubi H. A comprehensive review of nanofiitration membranes: treatment, pretreatment, modeling, and atomic force microscopy [J]. Desalination, 2004, 170(3): 281-308. 被引量:1
  • 4Hassan A M, AI-Soft M A K, AI-Amoudi A Set al. A new approach to membrane and thermal seawater desalination processes using nanoftltration membranes (Part 1) [J]. Desalination, 1998, 118(1-3): 35-51. 被引量:1
  • 5Hassan A M, Farooque A M, Jamaluddin A T Met al. A demonstration plant based on the new NF-SWRO process [J]. Desalination, 2000, 131(1-3): 157-171. 被引量:1
  • 6Sangho Lee, Chung-Hak Lee. Effect of operation conditions on CaSO4 scale formation mechanism in nanofiltration for water softening [J]. War Res, 2000, 34(15): 3854-3866. 被引量:1
  • 7Dydo Piotr, Turek Marian, Ciba Jerzy. Scaling analysis of nanofiltration systems fed with saturated calcium sulfate solutions in the presence of carbonate ions [J]. Desalination, 2003, 159(3): 245-251. 被引量:1
  • 8Seong Hoon Yoon, Chung Hak Lee, Kyu Jin kim et al. Effcet of calcium ion on the fouling of nanofilter by humic acid in drinking water production [J]. War Res, 1998, 32(7): 2180-2186. 被引量:1
  • 9Hrrsch P, Gorenflo A, Fuder C et al. Biofouling of ultra and nanofiltration membranes for drinking water treatment characterized by fluorescence in situ-hybridization (FISH) [J]. Desalination, 2005, 172(1): 41-52. 被引量:1
  • 10Seidel Arza, Elimelech Menachem. Coupling between chemical and physical interactions in natural organic matter (NOM) fouling of nanofiltration membranes: implications for fouling control [J]. J Membr Sci, 2002, 203(1-2): 245-255. 被引量:1

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