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- In relation to this article, we declare that there is no conflict of interest.
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Received January 24, 2014
Accepted February 27, 2014
- This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Deposition of toxic metal particles on rough nanofiltration membranes
Oluranti Agboola†
Jannie Maree1
Richard Mbaya
Caliphs Musa Zvinowanda1
Gomotsegang Fred Molelekwa2
Nora Jullok2
Bart Van der Bruggen2
Alexander Volodine3
Chris Van Haesendonck3
Department of Chemical Engineering, Tshwane University of Technology, Pretoria, South Africa 1Department of Environmental Water and Earth Science, Tshwane University of Technology, Pretoria, South Africa 2Process Engineering for Sustainable Systems, Department of Chemical Engineering, KU Leuven, W. de Croylaan 46, B-3001 Heverlee, Belgium 3Solid State Physics and Magnetism Section, KU Leuven, Celestijnenlaan 200d, Box 2414, B-3001 Heverlee, Belgium
sadikuo@tut.ac.za, funmi2406@gmail.com
Korean Journal of Chemical Engineering, August 2014, 31(8), 1413-1424(12), 10.1007/s11814-014-0075-6
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Abstract
Two nanofiltration (NF90 and Nano-Pro-3012) membranes were investigated for their capacity to remove metal ions. This study presents the effect of membrane roughness on the removal of toxic metal ions during dead end membrane filtration. Atomic force microscopy, scanning electron microscopy, WSXM software and ImageJ were used to characterize the roughness of the membranes. Gradual decrease in filtration permeate flux was observed as foulants_x000D_
accumulated at the interface of the membranes; filtration permeate flux varied from 20 L/m2/h to 14 L/m2/h and 11 L/m2/h to 6 L/m2/h for NF90 and Nano-Pro-3012, respectively. NF90 membrane was more prone to fouling than the Nano-Pro-3012 membrane: the percentage flux reduction was higher for NF90 (3.6%) than Nano-Pro-3012 (0.98%). The bearing ratio of the fouled NF90 exhibited a high peak of 7.09 nm than the fouled Nano-Pro-3012 with the peak of 6.8 nm.
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Skaug MJ, Faller R, Longo ML, J. Chem. Phys., 134, 1 (2011)
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Tamime R, Wyart Y, Siozade L, Baudin I, Deumie C, Glucina K, Moulin P, Membranes, 1, 91 (2011)
Pontie M, Thekkedath A, Kecili K, Dach H, De Nardi F, Castaing JB, Desalination, 292, 73 (2012)
Sader JE, Sanelli JA, Adamson BD, Monty JP, Wei X, Crawford SA, Friend JR, Marusic I, Mulvaney P, Bieskes J, Rev. Sci. Instrum., 83, 1 (2012)
Khulbe KC, Matsuura T, Polymer, 41(5), 1917 (2000)
Boussu K, Van der Bruggen B, Volodin A, Snauwaert J, Van Haesendonck C, Vandecasteele C, J. Colloid Interface Sci., 286(2), 632 (2005)
Stawikowska J, Livingston AG, J. Membr. Sci., 425, 58 (2013)
Song L, Johnson PR, Elimelech M, Environ. Sci. Technol., 28, 1164 (1994)
Song LF, Elimelech M, J. Colloid Interface Sci., 167(2), 301 (1994)
Brant JA, Johnson KM, Childress AE, Colloids Surf. A: Physicochem. Eng. Asp., 280, 45 (2006)
Boussu K, Belpaire A, Volodin A, Van Haesendonck C, Van der Meeren P, Vandecasteele C, Van der Bruggen B, J. Membr. Sci., 289(1-2), 220 (2007)
Schafer AI, Andritosos N, Karabelas AJ, Hoek EMV, Schneider R, Nystrom M, Fouling in nanofiltration, nanofiltration-principles and applications, Elsevier Advanced Technology, UK (2004).
Horcas I, Fernandez R, Gomez-Rodriguez JM, Colchero J, Gomez-Herrero J, Baro AM, Rev. Sci. Instrum., 78, 1 (2007)
Taylor JS, Thompson DM, Carswell JK, J. AWWA, 79, 72 (1987)
Chaudhari LB, Murthy ZVP, J. Environ. Res. Dev., 3, 400 (2008)
Vanysek P, Ionic conductivity and diffusion at infinite dilution in: CRC Handbook of Chemistry and Physics, 90th Ed., CRC Press, Boca Raton, Florida, 5 (2005).
Mohammad AW, Othaman R, Hilal N, Desalination, 168, 241 (2008)
Bowen WR, Hilal N, Lovitt RW, Wright CJ, J. Membr. Sci., 139(2), 269 (1998)