Please use this identifier to cite or link to this item: https://doi.org/10.1016/S0011-9164(03)00300-X
DC FieldValue
dc.titleEmergence of thermodynamic restriction and its implications for full-scale reverse osmosis processes
dc.contributor.authorSong, L.
dc.contributor.authorHu, J.Y.
dc.contributor.authorOng, S.L.
dc.contributor.authorNg, W.J.
dc.contributor.authorElimelech, M.
dc.contributor.authorWilf, M.
dc.date.accessioned2014-06-17T08:17:44Z
dc.date.available2014-06-17T08:17:44Z
dc.date.issued2003-07-10
dc.identifier.citationSong, L., Hu, J.Y., Ong, S.L., Ng, W.J., Elimelech, M., Wilf, M. (2003-07-10). Emergence of thermodynamic restriction and its implications for full-scale reverse osmosis processes. Desalination 155 (3) : 213-228. ScholarBank@NUS Repository. https://doi.org/10.1016/S0011-9164(03)00300-X
dc.identifier.issn00119164
dc.identifier.urihttp://scholarbank.nus.edu.sg/handle/10635/65525
dc.description.abstractThe production rate of permeate in a reverse osmosis (RO) process controlled by mass transfer is proportional to the net driving pressure and the total membrane surface area. This linear relationship may not be the only mechanism controlling the performance of a full-scale membrane process (typically a pressure vessel holding six 1-m-long modules in series) which utilizes highly permeable membranes. The mechanisms that control the performance of an RO process under various conditions were carefully examined in this study. It was demonstrated that thermodynamic equilibrium can impose a strong restriction on the performance of a full-scale RO process under certain circumstances. This thermodynamic restriction arises from the significant increase in osmotic pressure downstream of an RO membrane channel due to the accumulation of rejected salt within the RO channel as a result of permeate water production. Concentration polarization is shown to have a weaker influence on the full-scale RO process performance than the thermodynamic restriction. The behavior of the process under thermodynamic restriction is quite different from the corresponding behavior that is controlled by mass transfer. The transition pressure for an RO process to shift from a mass transfer controlled regime to a thermodynamically restricted regime was determined by the basic parameters of the full-scale RO process.
dc.description.urihttp://libproxy1.nus.edu.sg/login?url=http://dx.doi.org/10.1016/S0011-9164(03)00300-X
dc.sourceScopus
dc.subjectFull-scale RO
dc.subjectMass transfer
dc.subjectReverse osmosis
dc.subjectRO process design
dc.subjectRO process design performance
dc.subjectTheory
dc.subjectThermodynamic restriction
dc.typeArticle
dc.contributor.departmentCIVIL ENGINEERING
dc.description.doi10.1016/S0011-9164(03)00300-X
dc.description.sourcetitleDesalination
dc.description.volume155
dc.description.issue3
dc.description.page213-228
dc.description.codenDSLNA
dc.identifier.isiut000182871400001
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