Thin film nanocomposite forward osmosis membrane prepared by graphene oxide embedded PSf substrate

Document Type : Research Article

Authors

1 Department of Chemical Engineering, Faculty of Engineering, University of Isfahan, Isfahan, Iran

2 Department of Chemical Technologies, Iranian Research Organization for Science and Technology (IROST), Tehran, Iran

Abstract

One of the limiting factors in good performance of forward osmosis (FO) membranes is the internal concentration polarization (ICP). To reduce ICP, thin film nanocomposite forward osmosis (TFN-FO) membranes were fabricated by adding different amounts of graphene oxide (GO) nanoplates (0-1 wt. %) to polymer matrix of polysulfone (PSf) substrate. The prepared nanocomposite membranes exhibited both hydrophilicity and porosity higher than that of neat PSf counterpart. An optimum amount of 0.5 wt% was obtained for GO addition into the membranes. The corresponding fabricated thin film nanocomposite (TFN) membrane (TFNG0.5) revealed a water permeability of 2.44 L/m2hbar which is 66% higher compared to an in-house made composite membrane. The FO performance of TFN was assessed by DI water as feed solution and 1 M NaCl as draw solution in AL-DS orientation. The water flux of the synthesized FO membranes increased upon adding of GO nanoplates and reached to a maximum water flux of 37.74 (L/m2h) for TFNG0.5 membrane. This flux is about 3 times higher than TFC membranes without significant changes in their salt rejection. The higher water flux of the TFN membranes can be attributed to ICP decrease originating from reduction of structural parameter of the membranes.

Keywords


[1] S. Zhao, L. Zou, C.Y. Tang, D. Mulcahy, Recent developments in forward osmosis: Opportunities and challenges, Journal of Membrane Science, 396 (2012) 1-21.
[2] T.-S. Chung, S. Zhang, K.Y. Wang, J. Su, M.M. Ling, Forward osmosis processes: Yesterday, today and tomorrow, Desalination, 287 (2012) 78-81.
[3] H.-S.L.G.M. Geise, D.J. Miller, B.D. Freeman, J.E. Mcgrath, D.R. Paul, Water Purification by Membranes: The Role of Polymer Science, Journal of Polymer Science Part B: Polymer Physics, 48 (2010) 1685-1718.
[4] M.A. Shannon, P.W. Bohn, M. Elimelech, J.G. Georgiadis, B.J. Marinas, A.M. Mayes, Science and technology for water purification in the coming decades, Nature, 452 (2008) 301-310.
[5] M.M. Motsa, B.B. Mamba, A.D. Haese, E.M.V. Hoek, A.R.D. Verliefde, Organic fouling in forward osmosis membranes: The role of feed solution chemistry and membrane structural properties, Journal of Membrane Science, 460 (2014) 99-109.
[6] C. Charcosset, A review of membrane processes and renewable energies for desalination, Desalination, 245 (2009) 214-231.
[7] J. Dong, L. Li, T.M. Neoff, R. Lee, Desalination by reverse osmosis using MFI zeolite membranes, journal of Membrane Science, 243 (2004) 401-404.
[8] D. Mattai, K.P. Lee, T.C. Arnot, A review of reverse osmosis membrane materials for desalination – development to date and future potential, Journal of Membrane Science, 370 (2011) 1-22.
[9] O.A. Bamaga, A. Yokochi, B. Zabara, A.S. Babaqi, Hybrid FO/RO desalination system: preliminary assessment of osmotic energy recovery and designs of new FO membrane module configuration, Desalination, 268 (2011) 163-169.
[10] M. Elimelech, W.A. Phillip, The future of seawater desalination: energy, technology, and the environment, Science, 333 (2011) 712-717.
[11] E.M.V. Hoek, M.C.Y. Wong, K. Martinez, G.Z. Ramon, Impacts of operating conditions and solution chemistry on osmotic membrane structure and performance, Desalination, 287 (2012) 340-349.
[12] J.R. McCutcheon, R.L. McGinnis, M. Elimelech, Desalination by ammonia–carbon dioxide forward osmosis: Influence of draw and feed solution concentrations on process performance, Journal of Membrane Science, 278 (2006) 114-123.
[13] C. Suh, S. Lee, Modeling reverse draw solute flux in forward osmosis with external concentration polarization in both sides of the draw and feed solution, Journal of Membrane Science 427 (2013) 114-123.
[14] Z. Liu, H. Bai, J. Lee, D.D. Sun, A low-energy forward osmosis process to produce drinking water, Energy & Environmental Science 4(2011) 2582.
[15] R.L. McGinnis, M. Elimelech, Energy requirements of ammonia–carbon dioxide forward osmosis desalination, Desalination, 207 (2007) 370-382.
[16] C.R. Martinetti, A.E. Childress, T.Y. Cath, High recovery of concentrated RO brines using forward osmosis and membrane distillation, Journal of Membrane Science, 331 (2009) 31-39.
[17] S. Zhao, L. Zou, Effects of working temperature on separation performance, membrane scaling and cleaning in forward osmosis desalination, Desalination, 278 (2011) 157-164.
[18] A. Achilli, T.Y. Cath, E.A. Marchand, A.E. Childress, The forward osmosis membrane bioreactor: a low fouling alternative to MBR processes, Desalination, 239 (2009) 10-21.
[19] S. Lee, C. Boo, M. Elimelech, S. Hong, Comparison of fouling behavior in forward osmosis (FO) and reverse osmosis (RO), Journal of Membrane Science 365 (2010) 34-39.
[20] B. Mi, M. Elimelech, Organic fouling of forward osmosis membranes: Fouling reversibility and cleaning without chemical reagents, Journal of Membrane Science, 348 (2010) 337-345.
[21] Y. Gao, Y.-N. Wang, W. Li, C.Y. Tang, Characterization of internal and external concentration polarizations during forward osmosis processes, Desalination, 338 (2014) 65-73.
[22] J.R. McCutcheon, R.L. McGinnis, M. Elimelech, A novel ammonia-carbon dioxide forward (direct) osmosis desalination process, Desalination, 174 (2005) 1-11.
[23] C.Y. Tang, Q. She, W.C.L. Lay, R. Wang, A.G. Fane, Coupled effects of internal concentration polarization and fouling on flux behavior of forwar dosmosis membranes during humic acid filtration, Journal of Membrane Science 354 (2010) 123-133.
[24] G.T. Gray, J.R. McCutcheon, M. Elimelech, Internal concentration polarization in forward osmosis" role of membrane orientation, Desalination, 197 (2006) 1-8.
[25] J.R. McCutcheon, M. Elimelech, Influence of concentrative and dilutive internal concentration polarization on flux behavior in forward osmosis, Journal of Membrane Science, 284 (2006) 237-247.
[26] S. Loeb, L. Titelman, E. Korngold, J. Freiman, Effect of porous support fabric on osmosis through a Loeb-Sourirajan type asymmetric membrane, Journal of Membrane Science, 129 (1997) 243-249.
[27] N. Niksefat, M. Jahanshahi, A. Rahimpour, The effect of SiO2 nanoparticles on morphology and performance of thin film composite membranes for forward osmosis application, Desalination, 343 (2014) 140-146.
[28] M. Amini, M. Jahanshahi, A. Rahimpour, Synthesis of Novel Thin Film Nanocomposite (TFN) Forward Osmosis Membranes Using Functionalized Multi-walled Carbon Nanotubes, Journal of Membrane Science, 435 (2013) 233-241.