Aviso: para depositar documentos, por favor, inicia sesión e identifícate con tu cuenta de correo institucional de la UCM con el botón MI CUENTA UCM. No emplees la opción AUTENTICACIÓN CON CONTRASEÑA
 

Air gap membrane distillation: Desalination, modeling and optimization

dc.contributor.authorKhayet Souhaimi, Mohamed
dc.contributor.authorCojocaru, C.
dc.date.accessioned2023-06-20T03:41:30Z
dc.date.available2023-06-20T03:41:30Z
dc.date.issued2012-02-15
dc.description© 2011 Elsevier B.V. The authors are grateful to Spanish Ministry of Science and Innovation for supporting the research grant (project SB2009-0009) and the financial support of the University Complutense of Madrid, UCM-BSCH (Projects GR58/08 and GR35/10-A, UCM group 910336).
dc.description.abstractResponse surface methodology has been applied for modeling and optimization of air gap membrane distillation process used in desalination. Regression models have been developed to predict the performance index and the specific performance index that takes into consideration the energy consumption as function of different variables. The developed models have been statistically validated by analysis of variance. The rejection factors were found to be greater than 99.9%. Two optimal operating conditions have been determined for each response. For the performance index the optimal solution was a cooling inlet temperature of 13.9 degrees C, a feed inlet temperature of 71 degrees C and a feed flow rate of 183 L/h. Under these conditions the experimental performance index, 47.189 kg/m(2).h, was found to be the greatest value among all performed experiments. For the specific performance index, the optimal solution was also 13.9 degrees C cooling inlet temperature, 59 degrees C feed inlet temperature and 205 L/h feed flow rate. When applying these last optimum conditions, the obtained experimental specific performance index, 188.7 kg/kWh, was also found to be the highest value. This corresponds to a specific energy consumption of 5.3 kWh/m(3). In all cases, the experimental results are in good agreement with the predicted ones by the developed models.
dc.description.departmentDepto. de Estructura de la Materia, Física Térmica y Electrónica
dc.description.facultyFac. de Ciencias Físicas
dc.description.refereedTRUE
dc.description.sponsorshipSpanish Ministry of Science and Innovation
dc.description.sponsorshipUniversity Complutense of Madrid, UCM-BSCH
dc.description.statuspub
dc.eprint.idhttps://eprints.ucm.es/id/eprint/26012
dc.identifier.doi10.1016/j.desal.2011.09.017
dc.identifier.issn0011-9164
dc.identifier.officialurlhttp://dx.doi.org/10.1016/j.desal.2011.09.017
dc.identifier.relatedurlhttp://www.sciencedirect.com/
dc.identifier.urihttps://hdl.handle.net/20.500.14352/44255
dc.journal.titleDesalination
dc.language.isoeng
dc.page.final145
dc.page.initial138
dc.publisherElsevier Science Bv
dc.relation.projectIDSB2009-0009
dc.relation.projectIDGR58/08
dc.relation.projectIDGR35/10-A
dc.rights.accessRightsrestricted access
dc.subject.cdu536
dc.subject.keywordResponse-Surface Methodology
dc.subject.keywordDirect-Contact
dc.subject.ucmTermodinámica
dc.subject.unesco2213 Termodinámica
dc.titleAir gap membrane distillation: Desalination, modeling and optimization
dc.typejournal article
dc.volume.number287
dcterms.references[1] M. Khayet, Membranes and theoretical modeling of membrane distillation: a review, Adv. Colloid Interface Sci. 164 (1–2) (2011) 56–88. [2] A.M. Alklaibi, N. Lior, Comparative Study of direct contact and air gap membrane distillation processes, Ind. Eng. Chem. Res. 46 (2) (2007) 584–590. [3] A.M. Alklaibi, N. Lior, Transport analysis of air gap membrane distillation, J. Membr. Sci. 255 (1–2) (2005) 239–253. [4] C.M. Guijt, G.W. Meindersma, T. Reith, A.B. de Haan, Air gap membrane distillation: 2. Model validation and hollow fibre module performance analysis, Sep. Purif. Technol. 43 (3) (2005) 245–255. [5] F.A. Banat, J. Simandl, Desalination by membrane distillation: a parametric study, Sep. Sci. Technol. 33 (1998) 201–226. [6] A.S. Jonsson, R. Wimmerstedt, A.C. Harrysson, Membrane distillation: a theoretical study of evaporation through microporous membranes, Desalination 56 (1985) 237–249. [7] H. Chang, J.S. Liau, C.D. Ho, W.H. Wang, Simulation of membrane distillation modules for desalination by developing user's model on Aspen Plus platform, Desalination 249 (2009) 380–387. [8] M. Khayet, C. Cojocaru, G. Zakrzewska-Trznadel, Response surface modelling and optimization in pervaporation, J. Membr. Sci. 321 (2) (2008) 272–283. [9] M. Khayet, M. Essalhi, C. Armenta Déu, C. Cojocaru, N. Hilal, Optimization of solarpowered reverse osmosis desalination pilot plant using response surface methodology, Desalination 261 (3) (2010) 284–292. [10] M. Khayet, C. Cojocaru, C. García Payo, Application of response surface methodology and experimental design in direct contact membrane distillation, Ind. Eng. Chem. Res. 46 (17) (2007) 5673–5685. [11] S. Akhnazarova, V. Kafarov, Experiment Optimization in Chemistry and Chemical Engineering, Mir Publishers, Moscow, 1982. [12] R.H. Myers, D.C. Montgomery, Response Surface Methodology: Process and Product Optimization Using Designed Experiments, JohnWiley & Sons, New Jersey, 2002. [13] M.A. Bezerra, R.E. Santelli, E.P. Oliveira, L.S. Villar, L.A. Escaleira, Response surfacemethodology (RSM) as a tool for optimization in, analytical chemistry, Talanta 76 (2008) 965–977. [14] M. Khayet, C. Cojocaru, M. Essalhi, Artificial neural network modelling and response surface methodology of desalination by reverse osmosis, J. Membr. Sci. 368 (2011) 202–214. [15] L. Gazagnes, S. Cerneaux, M. Persin, E. Prouzet, A. Larbot, Desalination of sodium chloride and seawater with hydrophobic ceramic membranes, Desalination 217 (2007) 260–266. [16] J. Koschikowski, M. Wieghaus, M. Rommel, Solar thermal-driven desalination plants based on membrane distillation, Desalination 156 (2003) 295–304. [17] F. Banat, N. Jwaied, M. Rommel, J. Koschikowski, M. Weighaus, Desalination by a “compact SMADES” autonomous solar-powered membrane distillation unit, Desalination 217 (2007) 29–37. [18] F. Banat, N. Jwaied, M. Rommel, J. Koschikowski, M. Weighaus, Performance evaluation of the “large SMADES” autonomous desalination solar-driven membrane distillation plant in Aqaba, Jordan, Desalination 217 (2007) 17–28.
dspace.entity.typePublication
relation.isAuthorOfPublication8e32e718-0959-4e6c-9e04-891d3d43d640
relation.isAuthorOfPublication.latestForDiscovery8e32e718-0959-4e6c-9e04-891d3d43d640

Download

Original bundle

Now showing 1 - 1 of 1
Loading...
Thumbnail Image
Name:
khayetNO13.pdf
Size:
1.63 MB
Format:
Adobe Portable Document Format

Collections