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9 - Reverse osmosis and nanofiltration

Published online by Cambridge University Press:  05 July 2013

Greg Foley
Affiliation:
Dublin City University
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Summary

Introduction to reverse osmosis

Reverse osmosis (RO) is the membrane filtration of solutions of low molecular weight solutes, especially salts [1]. At this small scale, it is appropriate to discard the idea of the membrane having distinct pores but instead to view it as a matrix through which both the solvent and solute diffuse. Diffusion occurs through the space between the chains of the polymer from which the membrane is constructed. However, the membrane may contain a small number of defects resulting in the presence of some pores.

The ability of a species to diffuse through an RO membrane is typically controlled by charge effects rather than size and, consequently, RO is used extensively for desalination processes. It is also used for water softening, i.e., removal of cations, especially calcium, and in production of high purity water such as that required in electronics industries. Smaller scale RO units are often used to produce high purity water for laboratory purposes.

Just like ultrafiltration, the flux of pure water through RO membranes is partly limited by the osmotic pressure of the solution. Osmotic pressure is a colligative property, meaning that at a fixed mass concentration, it increases as the molecular weight of the solute decreases. In other words, the osmotic pressure depends on the number of solute molecules per unit volume. Thus, the osmotic pressures of salt solutions are much greater than those of macromolecular solutions at the same molar concentration. This contributes to the need for the very high pressures, up to 100 bar, that are used in RO.

Type
Chapter
Information
Membrane Filtration
A Problem Solving Approach with MATLAB
, pp. 253 - 272
Publisher: Cambridge University Press
Print publication year: 2013

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References

Kucera, J. (2010). Reverse Osmosis. Industrial Applications and Processes. Wiley-Scrivener, Massachusetts, USA.Google Scholar
Wijmanns, J.G. and Baker, R.W. (1995). The solution-diffusion model: a review. Journal of Membrane Science, 107, 1–21.CrossRefGoogle Scholar
The van't Hoff / Morse equation is empirical in origin but can be derived from chemical thermodynamics. Actually, the technical difference between the van't Hoff and Morse equations is that in Morse, the concentrations should be expressed in molalities rather than molarities. However, this distinction is often forgotten. More information can be found in the following source: Dao, V.N.T., Morris, P.H. and Dux, P.F. (2008). On equations for the total suction and its matric and osmotic components. Cement and Concrete Research, 38, 1302–1305.
Shafer, A.I., Fane, A.G. and Waite, T.D. (Eds.) (2006). Nanofiltration. Principles and Applications. Elsevier, Oxford, UK.Google Scholar
Prausnitz, J.M., Lichtenhaler, R.N. and Gomes de Azevedo, E. (1998). Molecular Thermodynamics of Fluid-phase Equilibria, 3rd Edition. Prentice Hall, NJ, USA.Google Scholar
Rautenbach, R., and Albrecht, R. (1989). Membrane Processes. Wiley, New York, USA.Google Scholar
Sablani, S.S., Goosen, M.F.A., Al-Belushi, R. and Wilf, M. (2001). Concentration polarization in ultrafiltration and reverse osmosis: a critical review. Desalination, 141, 269–289.CrossRefGoogle Scholar
Soltanieh, M., and Gill, W. (1981). Review of reverse osmosis membranes and transport models. Chemical Engineering Communications, 12, 279–363.CrossRefGoogle Scholar

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