Studies on desalination performance of nanofiltration membranes and its application to seawater desalination

Expand
  • The College of Chemistry and Chemical Engineering, Ocean University of China, Qingdao 266003, China

Received date: 2005-10-27

  Revised date: 2005-10-27

  Online published: 2010-10-01

Abstract

Desalination experiments of four inorganic salt solutions (NaCl, Na2SO4, MgCl2, MgSO4) have been carried out by using a kind of nanofiltration membranes(ESNA1). The effects of the species and the concentration of salts as well as the operation pressure on the separation performance and the stability of nanofiltration membranes desalination have been investigated. Some rules of the desalination with nanofiltration membranes are gained. Studies on desalination performance of artificial seawater and seawater are also introduced. Results from the desalination of inorganic salt solutions show that salt rejection increases with the increase of operational pressure, while decreased with the increase of salt concentration. Furthermore, operational pressure and salt concentration made more effect on salt rejection of univalent salt solutions than on that of bivalent salt solutions. Results from artificial seawater and seawater desalination show that ESNA1 membrane is stable during the experiment and the flux is high under lowoperational pressure. What’s more, for all of the ions(Ca2+,Mg2+, SO42-),ESNA1 could achieved salt rejections up to 90%. The preliminary estimation considers that this nanofiltration membrane could be used to pretreat seawater.

Cite this article

Wang Yuhong, Su Baowei, Xu Jia, Ruan Guoling, Gao Congjie . Studies on desalination performance of nanofiltration membranes and its application to seawater desalination[J]. Industrial Water Treatment, 2006 , 26(2) : 46 -49 . DOI: 10.11894/1005-829x.2006年.26(02).46

References

[1] Petersen R J. Composite reverse osmosis and nanofiltration membranes [J]. J. Membr. Sci., 1993, 83(1): 81-150.
[2] 高从堦, 陈国华. 海水淡化技术与工程手册
[M]. 北京: 化学工业 出版社, 2004: 135-138.
[3] Hilal N, Al-Zoubi H, Darwish N A, et al. A comprehensive review of nanofiltration membranes: Treatment, pretreatment, modeling, and atomic force microscopy[J]. Desalination, 2004, 170(2): 281-308.
[4] Hassan A M. A new approach to membrane and thermal seawater desalination processes using nanofiltration membranes (Part 1) [J]. Desalination, 1998, 118(1): 35-51.
[5] Al-Shammir M, Ahmed M, Al-Rageeb M. Nanofiltration and calcium sulfate limitation for top brinetemperature in Gulf desalination plants[J]. J. Desalination, 2004, 167(2): 335-346.
[6] Hassan AM,Farooque AM,Jamaluddin ATM,et al. Ademonstration plant based on the new NF-SWRO process[J]. Desalination, 2000, 131(1): 157-171.
[7] Al-Sofi M A K, Hassan A M, Mustafa M, et al. Nanofiltration as a means ofachievinghigher TBTof≥ 120 ℃in MSF[J]. Desalination, 1998, 118(1): 123-129.
[8] 王晓琳. 纳滤膜分离技术最新进展[J]. 天津城市建设学院学报, 2003, 9(2): 1-3.
[9] 任建新. 膜分离技术及其应用
[M].北京: 化学工业出版社, 2003: 6-7.

Outlines

/