Abstract
The performance of FO is predicted numerically by one-dimensional model. Mass balance equation for the feed and draw side are coupled with the water flux model considering concentration polarization. Results of the present study showed the flow rate of the feed and draw solution should be determined by considering the water flux and the water recovery efficiency. Using the draw solution of as high concentration as possible is helpful to improve the water flux. As increasing the membrane module length, the averaged water flux per membrane length decreases but the water production increases. Therefore, in order to determine the membrane length, it is required to consider the water flux reduction, total water production, membrane size and the number of membrane. The water flux of counter-current flow is about 10% higher than that of co-current flow. Forming feed solution into series and draw solution into rows are effective in increasing water flux.
Similar content being viewed by others
References
J. C. Glenn, T. J. Gordon and E. Florescu, 2011 State of the Future Report, UN (2011).
The united nations world water development report, UNESCO (2011).
P. H. Gleick, Water resources, In Encyclopedia of climate and weather, Oxford University Press, New York, (1996).
H. Chung, S. Wibowo, B. Fajar, Y. Shin and H. Jeong, Study on low pressure evaporation of fresh water generation system model, The Journal of Mechanical Science and Technology, 26(2) (2012) 421–426.
A. Kalendar, T. Galal, A. Al-Saftawi and M. Zedan, Enhanced tubing thermal performance for innovative MSF system, The Journal of Mechanical Science and Technology, 25(8) (2011) 1969–1977.
T. Galal, A. Kalendar, A. Al-Saftawi and M. Zedan, Heat transfer performance of condenser tubes in an MSF desalination system, The Journal of Mechanical Science and Technology, 24(11) (2010) 2347–2355.
K. V. Reddy and N. Ghaffour, Overview of the cost of desalinated water and costing methodologies, Desalination, 205(1–3) (2007) 340–353.
A. von Gottberg, A. P. Pang and J. L. Talavera, Optimizing Water Recovery and Energy Consumption for Seawater RO Systems, GE Water & Process Technologies (2005).
J. MacHarg, T. F. Seacord and B. Sessions, ADC baseline tests reveal trends in membrane performance, Desalination & Water Reuse, 18(2) (2008) 30–39.
B. Mi and M. Elimelech, Organic fouling of forward osmosis membranes: Fouling reversibility and cleaning without chemical reagents, Journal of membrane science, 348(1–2) (2010) 337–345.
A. Achilli, T. Y. Cath and A. E. Childress, Power generation with pressure retarded osmosis: An experimental and theoretical investigation, Journal of membrane science, 343(1–2) (2009) 42–52.
O. S. Skramesto, S. E. Skilhagen and W. K. Nielsen, Power production based on osmotic pressure, Waterpower (2009).
G. T. Gray, J. R. McCutcheon and M. Elimelech, Internal concentration polarization in forward osmosis: role of membrane orientation, Desalination, 197(1–3) (2006) 1–8.
J. R. MeCutcheon and M. Elimelech, Influence of concentrative and dilutive internal concentration polarization on flux behavior in forward osmosis, Journal of Membrane, Science, Journal of membrane science, 284(1–2) (2006) 237–247.
N. Y. Yip, A. Tiraferri, W. A. Phillip, J. D. Schiffman, L. A. Hoover, Y. C Kim and M. Elimelech, Thin-film composite pressure retarded osmosis membranes for sustainable power generation from salinity gradients, Environmental Science & Technology, 45(10) (2011) 4360–4369.
D. Xiao, W. Li, S. Chou, R. Wang and C. Y. Tang, A modeling investigation on optimizing the design of forward osmosis hollow fiber modules, Journal of membrane science, 392–393 (2012) 76–87.
R. Wang, L. Shi, C. Y. Tang, S. Chou, C. Qiu and A. G. Fane, Characterization of novel forward osmosis hollow fiber membranes, Journal of membrane science, 355(1–2) (2010) 158–167.
E. M. Garcia-Castello, J. R. McCutcheon and M. Elimelech, Performance evaluation of sucrose concentration using forward osmosis, Journal of membrane science, 338(1–2) (2009) 61–66.
R. A. Robinson and R. H. Stokes, Electrolyte solutions, Dover Publications, Inc, Mineola, New York (2002).
B. S. Sparrow, Empirical equations for the thermodynamic properties of aqueous sodium chloride, Desalination, 159(2) (2003) 161–170.
C. H. Hsu and M. H. Li, Densities of aqueous blended amines, Journal of Chemical & Engineering Data, 42(3) (1997) 502–507.
F. Chenlo, R. Moreira, G. Pereira and B. Bello, Kinematic viscosity and water activity of aqueous solutions of glycerol and sodium chloride, European food research and technology, 219(4) (2004) 403–408.
C. H. Tan and H. Y. Ng, Modified models to predict flux behavior in forward osmosis in consideration of external and internal concentration polarizations, Journal of Membrane science, 324(1–2) (2008) 209–219.
Author information
Authors and Affiliations
Corresponding author
Additional information
Recommended by Associate Editor Jae Dong Chung
Sung-Min Shim graduated from Hanyang University with a major in Mechanical Engineering in 2003. Now, he is a Ph.D. candidate at the Department of Mechanical Engineering of Hanyang University and is working for STX Institute of Technology as a researcher.
Woo-Seung Kim graduated from Hanyang University with a major in Mechanical Engineering in 1981. He got a Ph.D at North Carolina State University in 1989. Prof. Kim is the director of the Office of Industry-University Foundation at Hanyang University. He is currently interested in the research topics of desalination and CCS.
Rights and permissions
About this article
Cite this article
Shim, SM., Kim, WS. A numerical study on the performance prediction of forward osmosis process. J Mech Sci Technol 27, 1179–1189 (2013). https://doi.org/10.1007/s12206-013-0305-6
Received:
Revised:
Accepted:
Published:
Issue Date:
DOI: https://doi.org/10.1007/s12206-013-0305-6