Please use this identifier to cite or link to this item: https://hdl.handle.net/10356/79612
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dc.contributor.authorGuan, Guoqiangen
dc.contributor.authorYang, Xingen
dc.contributor.authorWang, Rongen
dc.contributor.authorField, Roberten
dc.contributor.authorFane, Anthony Gordonen
dc.date.accessioned2014-06-10T02:08:57Zen
dc.date.accessioned2019-12-06T13:29:20Z-
dc.date.available2014-06-10T02:08:57Zen
dc.date.available2019-12-06T13:29:20Z-
dc.date.copyright2014en
dc.date.issued2014en
dc.identifier.citationGuan, G., Yang, X., Wang, R., Field, R., & Fane, A. G. (2014). Evaluation of hollow fiber-based direct contact and vacuum membrane distillation systems using aspen process simulation. Journal of Membrane Science, 464, 127-139.en
dc.identifier.issn0376-7388en
dc.identifier.urihttps://hdl.handle.net/10356/79612-
dc.description.abstractAmong four membrane distillation (MD) configurations, direct contact MD (DCMD) and vacuum MD (VMD) exhibit attractive characteristics from different perspectives and have great potential in treating reverse osmosis (RO) brine. Aiming at establishing a quick approach to predict the key output parameters associated with MD module performance and process efficiency, Aspen plus was employed to conduct systematic evaluation for both DCMD and VMD. Due to the lack of built-in MD operation models in Aspen Plus, one dimensional transport models were developed and complied as user customized units to simulate the hollow fiber-based DCMD and VMD modules. The corresponding programming was coded in FORTRAN language. The mathematical models for DCMD and VMD were verified by comparing the simulations results with the experimental and literature data, respectively. By incorporating the boundary-layer effect into the newly-established transport models, steady-state simulations of the respective DCMD and VMD flowsheets were carried out. The results showed that the DCMD presented much lower process efficiency than VMD in terms of permeation flux and specific energy consumption per kg distillate generated, even though it is considered as the simplest and most commonly employed configuration. With the same module specifications and operating conditions at equivalent energy cost, the VMD system demonstrated a minimal 2.5-fold higher average vapor flux (e.g., water recovery capacity) when compared to DCMD. The fundamental difference between the two configurations was revealed through MD mass- and heat-transfer analysis. Based on simulated temperature profiles, it was found that the VMD configuration presented a much higher driving force (transmembrane temperature difference) and negligible conductive heat loss to the membrane, which is a promising feature for achieving high thermal efficiency.en
dc.language.isoenen
dc.relation.ispartofseriesJournal of membrane scienceen
dc.rights© 2014 Elsevier Ltd. This is the author created version of a work that has been peer reviewed and accepted for publication by Journal of Membrane Science, Elsevier Ltd. It incorporates referee’s comments but changes resulting from the publishing process, such as copyediting, structural formatting, may not be reflected in this document. The published version is available at: [http://dx.doi.org/10.1016/j.memsci.2014.03.054].en
dc.subjectDRNTU::Engineering::Environmental engineering::Water treatmenten
dc.titleEvaluation of hollow fiber-based direct contact and vacuum membrane distillation systems using aspen process simulationen
dc.typeJournal Articleen
dc.contributor.schoolSchool of Civil and Environmental Engineeringen
dc.contributor.researchSingapore Membrane Technology Centreen
dc.identifier.doi10.1016/j.memsci.2014.03.054en
dc.description.versionAccepted versionen
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