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Received March 16, 2016
Accepted October 24, 2016
- 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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Modeling of reverse osmosis flux of aqueous solution containing glucose
1Water, Membranes and Environmental Biotechnology Laboratory, CERTE, BP 273, Soliman 8020, Tunisia 2Alliance for Research on North Africa (ARENA), 1-1-1 Tennodai Tsukuba, Ibaraki 305-8572, Japan 3National Food Research Institute, Ministry of Agriculture, Forestry and Fisheries, Tsukuba, Ibaraki 305, Japan 4, Tunisia
amor.hafiane@certe.rnrt.tn
Korean Journal of Chemical Engineering, February 2017, 34(2), 407-412(6), 10.1007/s11814-016-0298-9
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Abstract
The aim of the paper is to model the permeate flux during reverse osmosis (RO) of a highly concentrated glucose solution using the osmotic pressure model. Such a model accounts for the effect of the concentration polarization phenomenon on the permeate flux. To apply this model the viscosity, the osmotic pressure of solution and the diffusion coefficient of glucose were estimated. Using mathematical simulation software, the values of mass transfer coefficient for different concentrations of glucose (5, 10, 15 and 20 wt%) and at different feed flow rate were determined. The experimental permeate flux values conducted on flat RO membranes (Type HR-99) agreed well with the values calculated by the osmotic pressure model, as shown by statistical analysis.
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Sundaramoorthy S, Srinivasan G, Murthy DVR, Desalination, 277(1-3), 257 (2011)
Kostoglou M, Karabelas AJ, Desalination, 316, 91 (2013)
Hung LY, Lue SJ, You JH, Desalination, 265(1-3), 67 (2011)
Lopes GH, Chavez BB, Ibaseta N, Guichardon P, Haldenwang P, Procedia Eng., 44, 1934 (2012)
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