JWARP  Vol.1 No.3 , September 2009
Pilot Study of Ultrafiltration-Nanofiltration Process for the Treatment of Raw Water from Huangpu River in China
ABSTRACT
Pilot-scale test was carried out to evaluate the performance of a combined ultrafiltration (UF)-nanofiltration (NF) membrane process for the treatment of raw water from Huangpu River, Shanghai, in China. Results showed that UF could significantly remove turbidity, iron and manganese, and also could retain a part of high molecular weight (MW) organic compounds. Subsequently, NF could further reject low MW organics and inorganic salts, and ensured the treated water to reach the Standards for Drinking Water Quality in China. It seemed that 90 L/m2&#183h was an appropriate permeate flux for UF system when the raw water was directly filtered by UF membrane, the addition of coagulant (alum or ferric chloride) was not preferable to mitigate the fouling of the UF membrane. After near 120 days operation, the permeate flux of NF could be main-tained at 24-25 L/m2&#183h steadily, and no chemical clean was required.

Cite this paper
J. ZHOU, N. GAO, G. PENG and Y. DENG, "Pilot Study of Ultrafiltration-Nanofiltration Process for the Treatment of Raw Water from Huangpu River in China," Journal of Water Resource and Protection, Vol. 1 No. 3, 2009, pp. 203-209. doi: 10.4236/jwarp.2009.13025.
References
[1]   Y. Magara, S. Kunikane, and M. Itoh, “Advanced membrane technology for application to water treatment,” Wat Sci Tech , Vol. 37, pp. 91–99, October 1998.

[2]   AWWA Membrane technology research committee, “Committee report: Membrane process,” JAWWA, Vol. 90, pp. 91–105, June 1998.

[3]   S. Kunikane, M. lton, and Y. Magara, “Advanced membrane technology of application to water treatment,” Water Supply, Vol. 16, pp. 313–318, January 1998.

[4]   Amy, L. Gary, Collins, R. Michael, Kuo, C. James, King, and H. Paul, “Comparing gel permeation chromatography and ultrafiltration for the molecular weight characterization of aquatic organic matter,” J. AWWA, Vol. 79, pp. 43–39, January 1987.

[5]   W. Liu, H. Wu, Z. Wang, S. L. Ong, J. Y. Hu and W. J. Ng, “Investigation of assimilable organic carbon (AOC) and bacterial regrowth in drinking water distribution system,” Water Research, Vol. 36, pp. 891–898. February 2002.

[6]   D. Van der Kooij, W. A. M. Hijnen, and A. Visser, “Determining the concentration of easily assimilable organic carbon in drinking water,” J. AWWA, Vol. 74, pp. 540–545, October 1982.

[7]   P. M. Huck, “Measurement of biodegradable organic matter and bacterial growth potential in drinking water,” J. AWWA, Vol. 82, pp. 78–86, July 1990.

[8]   N. Park, B. Kwon, M. Sun, H. Ahn, C. Kim, C. Kwoak, D. Lee, S. Chae, H. Hyung, and J. Cho, “Application of various membranes to remove NOM typically occurring in Korea with respect to DBP, AOC and transport parameters,” Desalination, Vol. 178, pp. 161–169, July 2005.

[9]   C. Cabassud, C. Anselme, and J. J. Bersillon, “Ultrafiltration as a non-polluting alternative to traditional clarification in water treatment,” Filtration &separation, Vol. 28, pp.194–198, July 1999.

[10]   Z. Wang, J. M. Yao, C. Zhou and J. S Chu, “The influence of various operating conditions on the permeation flux during dead-end microfiltration,” Desalination, Vol. 212, pp. 209–218, June 2007.

[11]   C. Guigui, J. C. Rouch, L. Durand-Bourlier, V. Bonnelye and P. Aptel, “Impact of coagulation conditions on the in-line coagulation/UF process for drinking water production,” Desalination, Vol. 147, pp. 95–100, September 2002.

[12]   L. T. Veornique, R. W. Mark, J. Y. Bottero et al, “Coagulation pretreatment for ultrafiltration of a surface water, JAWWA, Vol. 82, pp. 76–81, December 1990.

[13]   K. Khatib, J. Rose, O. Barres, W. Stone, J. Y. Bottero, and C. Anselme, “Physico-chemical study of fouling membrane mechanisms of ultrafiltration membrane on Biwa Lake(Japan),” Jour Membrane Science, Vol. 130, pp. 53 –62, July 1997.

 
 
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