TY - JOUR
T1 - Treatment of high salinity solutions
T2 - Application of air gap membrane distillation
AU - Alkhudhiri, Abdullah
AU - Darwish, Naif
AU - Hilal, Nidal
N1 - Funding Information:
Authors would like to thank King Abdul Aziz City for Science and Technology (KACST) for funding A. Alkhudhiri.
Copyright:
Copyright 2012 Elsevier B.V., All rights reserved.
PY - 2012/11/15
Y1 - 2012/11/15
N2 - Air Gap Membrane Distillation, using a high concentration of NaCl, MgCl 2, Na 2CO 3, and Na 2SO 4, is implemented in this study. Permeate fluxes are measured for different feed concentrations and membrane pore sizes (0.2 and 0.45μm). The flux declines as the concentration of salt increases, and increases as the pore size increases. The TF200 membrane showed excellent hydrophobicity compared to TF450. Moreover, the energy consumption was measured at different salt concentrations for the different membrane sizes, and was found to be independent of membrane pore size, salt type and salt concentration in the feed solution.
AB - Air Gap Membrane Distillation, using a high concentration of NaCl, MgCl 2, Na 2CO 3, and Na 2SO 4, is implemented in this study. Permeate fluxes are measured for different feed concentrations and membrane pore sizes (0.2 and 0.45μm). The flux declines as the concentration of salt increases, and increases as the pore size increases. The TF200 membrane showed excellent hydrophobicity compared to TF450. Moreover, the energy consumption was measured at different salt concentrations for the different membrane sizes, and was found to be independent of membrane pore size, salt type and salt concentration in the feed solution.
KW - Air Gap Membrane Distillation (AGMD)
KW - Desalination
KW - High concentration solution
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U2 - 10.1016/j.desal.2011.08.056
DO - 10.1016/j.desal.2011.08.056
M3 - Article
AN - SCOPUS:84856572069
SN - 0011-9164
VL - 287
SP - 55
EP - 60
JO - Desalination
JF - Desalination
ER -